System and method for dry forming zoned absorbent cores

ABSTRACT

An apparatus and method for depositing particulate matter onto a supply of absorbent core fibrous substrate material are disclosed. The apparatus has a feed tray that has an inlet for receiving a supply of particulate matter. At least part of a lower pan of the feed tray is a slideable shuttle pan that has an outlet edge located near a supply of absorbent core fibrous substrate material that is moving in a machine direction. The supply of particulate matter passes over the outlet edge to exit the feed tray. A mechanism operates the shuttle pan through a range of motion having a forward stroke and a backward stroke. During the forward stroke, the outlet edge follows the supply of absorbent core fibrous substrate material.

FIELD OF THE INVENTION

[0001] The present invention relates generally to systems and methodsfor manufacturing absorbent garment cores. More specifically, thepresent invention relates to a system and method for providing zoneddisposition of superabsorbent particles and other particulate andfibrous additives into an absorbent core fibrous substrate material.

BACKGROUND OF THE INVENTION

[0002] Disposable absorbent garments such as infant diapers or trainingpants, adult incontinence products and other such products typicallywere constructed with a moisture-impervious outer backsheet, amoisture-pervious body-contacting inner topsheet, and amoisture-absorbent core sandwiched between the liner and backsheet.

[0003] Much effort has been expended to find cost-effective materialsfor absorbent cores that display good liquid absorbency and retention.Particles of superabsorbent materials (SAP) in the form of granules,beads, fibers, bits of film, globules, etc., have been favored for suchpurposes. Such SAP materials generally are polymeric gelling materialsthat are capable of absorbing and retaining even under moderate pressurelarge quantities of liquid, such as water and body wastes, relative totheir weight. The SAP particles typically have been distributed within afibrous web of fluffed pulp material, which may comprise natural orsynthetic fibers. Such absorbent structures are commonly referred to asfluff pulp/SAP cores.

[0004] Superabsorbent material generally is a water-insoluble butwater-swellable polymeric substance capable of absorbing water in anamount that is at least ten times the weight of the substance in its dryform. In one type of superabsorbent material, the particles may bedescribed chemically as having a back bone of natural or syntheticpolymers with hydrophilic groups or polymers containing hydrophilicgroups being chemically bonded to the back bone or an intimate admixturetherewith. Included in this class of materials are modified polymerssuch as sodium neutralized cross-linked polyacrylates andpolysaccharides including, for example, cellulose and starch andregenerated cellulose that are modified to be carboxylated,phosphonoalkylated, sulphoxylated or phosphorylated, causing the SAP tobe highly hydrophilic. Such modified polymers also may be cross-linkedto reduce their water-solubility.

[0005] The ability of a superabsorbent material to absorb liquid isdependent upon the form, position and/or manner in which particles ofthe superabsorbent material are incorporated into the fibrous web of theabsorbent core. Whenever a particle of the superabsorbent material iswetted, it swells and forms a gel. Gel formation can block liquidtransmission into the interior of the absorbent core, a phenomenoncalled “gel blocking.” Gel blocking prevents liquid from rapidlydiffusing or wicking past the “blocking” particles of superabsorbent,causing portions of a partially hydrated core to become inaccessible tomultiple doses of urine. Further absorption of liquid by the absorbentcore must then take place via a diffusion process. This is typicallymuch slower than the rate at which liquid is applied to the core. Gelblocking often leads to leakage from the absorbent article well beforeall of the absorbent material in the core is fully saturated.

[0006] Despite the incidence of gel blocking, superabsorbent materialsare commonly incorporated into absorbent cores because they absorb andretain large quantities of liquid, even under load. However, in orderfor superabsorbent materials to function, the liquid being absorbed inthe absorbent structure must be transported to unsaturatedsuperabsorbent material. In other words, the superabsorbent materialmust be placed in a position to be contacted by liquid. Furthermore, asthe superabsorbent material absorbs the liquid it must be allowed toswell. If the superabsorbent material is prevented from swelling, suchas by being tightly constrained within the fibrous web or by pressureexerted by the swelling of adjacent superabsorbent particles, it willcease absorbing liquids.

[0007] Adequate absorbency of liquid by the absorbent core at the pointof initial liquid contact and rapid distribution of liquid away fromthis point are necessary to ensure that the absorbent core hassufficient capacity to absorb subsequently deposited liquids. Previousabsorbent cores have thus attempted to absorb quickly and distributelarge quantities of liquids throughout the absorbent core whileminimizing gel blocking during absorption of multiple doses of liquid.

[0008] Some of the more important performance attributes of an absorbentcore of a diaper (or any other absorbent garment) are functionalcapacity, rate of absorption, and core stability in use. Absorptionunder load or AUL is a good measure of functional capacity and the rateat which that absorption occurs. AUL is a function of both SAP basisweight (mass per unit area) and the composition of SAP used in thecomposite. Conventional baby diaper cores that contain only a fibrousweb of fluff pulp and a high gel strength SAP typically maintainadequate SAP efficiency if the core contains less than about 50% SAP.Fluff/SAP diaper cores containing more than 50% SAP generally result inlower SAP efficiency because of gel blocking. Although fluff/SAP coresat greater than 50% SAP can provide adequate absorbency, the overallbasis weight of the core typically must be increased to compensate forthe lower efficiency of the SAP. Increasing the basis weight decreasesthe performance/cost ratio of the absorbent core, making themuneconomical. Also, increased basis weights tend to affect the fit andcomfort of the garment, as well as impacting the packaging and shippingcosts.

[0009] Attempts to increase the relative weight of SAP by reducing thebasis weight of the conventional fluff pulp have resulted in failurebecause low density fluff pulp mats have been unable to withstand thetensile loads placed on them during the manufacturing process. Suchcores also exhibit poor wet strength, making them unstable during use,and fail to adequately secure the SAP in place. The introduction ofrelatively high integrity fibrous structure cores, however, has allowedthe basis weight of the fibrous web to be decreased without compromisingthe manufacturability and wet strength of the absorbent core. Theseabsorbent core structures have improved SAP efficiency and a loweroverall basis weight. Such absorbent cores are disclosed, for example,in U.S. Statutory Invention Registration No. H1,565 to Brodof et al.,which is incorporated by reference herein in its entirety and in amanner consistent with the present invention. These high integrityfibrous structure cores, referred to herein as “tow/SAP” cores or“tow-based” cores, typically use a continuous tow of crimped filaments.The tow may be provided to the absorbent core manufacturer in a compactform and “opened” (i.e., “bloomed” or fluffed up) prior to beingassembled into an absorbent core.

[0010] In some cases, the fibrous web of the tow/SAP core may be treatedwith a tackifying agent to adhere the SAP particles to the fibrous web.In other cases, the SAP particles may be introduced into the fibrous webwithout any adhesive, binder or tackifying agent, such as is disclosedin U.S. Pat. No. 6,068,620 issued to Chmielewski et al., which isincorporated by reference herein in its entirety and in a mannerconsistent with the present invention. Such a construction has beenreferred to as a dry-formed composite (DFC) core. A DFC core may besurrounded by a tissue layer or multiple tissue layers to form a DFClaminate structure that contains the fibrous web and SAP.

[0011] A problem with SAP-containing fibrous cores has been to providethe SAP into the fibrous web in a controlled manner. Typical knownprocesses for creating a conventional fluff pulp/SAP core use a largeforming chamber to blend the SAP with the fluffed pulp, then convey thisblend onto a drum or screen by using a vacuum. The drum or screen hasforming pockets that form the fluff pulp/SAP material into the desiredshape and the formed cores then are deposited for integration intoabsorbent products. Such methods have been found to be inefficientduring startup and transitions in the manufacturing line speed becausethey require a relatively large amount of time to provide a stabilizedmixture of SAP and fluff pulp, leading to the creation of a large numberof scrap products until stabilization.

[0012] Other conventional processes for forming fluff pulp/SAP coresimmerse the fluffed pulp in a fluid mixture containing SAP particles,then dry the fluff pulp/SAP mixture before integration into theabsorbent article. Such wet forming processes typically require moremanufacturing steps and are more expensive than dry forming methods.

[0013] Other feeding systems use fixed-size moving mechanical gates thatprovide a uniform amount of SAP to the absorbent core, such as isdisclosed in U.S. Pat. No. 6,139,912 to Onuschak et al., which isincorporated herein by reference in its entirety and in a mannerconsistent with the present invention. Although such devices may besuitable for providing an even flow of SAP or other powdered andparticulate additives to absorbent cores, they rely on relativelycomplex feeding machinery, including a rotary valve that uses apneumatic SAP conveyor to return undistributed SAP back to a supplycontainer. Pneumatic conveyors typically require a relatively long timeto become pressurized and to convey the SAP, causing inefficienciesduring transitional phases, such as when the machine operating speedvaries, such as during start-up and shut-down, or when it is desired tochange the amount of SAP being fed to the core. The additional parts ofsuch feeders may also be expensive and subject to wear and other serviceproblems. Similar devices, having similar deficiencies, are disclosed inU.S. Pat. No. 4,800,102 to Takada, which is incorporated herein byreference in its entirety and in a manner consistent with the presentinvention.

[0014] Still other feeding systems use pneumatic particle projectorsthat use pressurized gas to convey the SAP to the surface of theabsorbent core. Such devices are disclosed, for example, in U.S. Pat.Nos. 5,614,147 to Pelley and 5,558,713 to Siegfried et al., which areincorporated herein by reference in their entirety and in a mannerconsistent with the present invention. Such systems rely on relativelycomplex air conveyors, that may be susceptible to blockage and may notefficiently accommodate as wide a variety of particulate, powder andfibrous materials as other systems due to their relatively small passagesizes. Indeed, it has been found that the compressed air used in suchpneumatic conveyors is often contaminated with oil that may causeblockage, SAP degradation, and other problems. Such systems may alsorequire a relatively long time to stabilize, leading to inefficienciesduring transitional phases.

[0015] Other known SAP feeding systems are disadvantageous for a numberof reasons. First, the mixture of fiber and SAP still is subject tolocal concentrations and shortages of SAP. Second, these feeding systemstypically can not be controlled accurately enough to provideconcentrations and shortages of SAP when they are desired. Third, suchfeeding systems can not be controlled to accurately provide reduced SAPamounts that are necessary during transitional phases, leading toimproperly loaded cores during those phases of operation.

[0016] These are just a few of the disadvantages of the prior art whichthe preferred embodiments seek to address. The foregoing description ofcertain material, methods and systems with their attendant disadvantagesin no way is meant to infer that the present invention excludes suchmaterials, methods, and systems. Indeed, certain embodiments of theinvention solve some of the aforementioned disadvantages, yet utilizethe same or similar materials, methods and/or systems.

SUMMARY OF THE INVENTION

[0017] It would be desirable to provide an apparatus and method forforming absorbent cores having zoned regions having relatively highconcentrations of particulate additives. Still further, it would bedesirable for such an apparatus and method to be efficient, easy tooperate, capable of operating with a variety of particulate matterfeeding devices, and capable of operating at high line speeds.

[0018] In accordance with these and other features of variousembodiments of the invention, there is provided an apparatus and methodfor depositing zoned particulate matter onto a supply of absorbent corefibrous substrate material moving in a machine direction having a feedtray that has an inlet for receiving a supply of particulate matter. Allor part of a lower pan of the feed tray is a slideable shuttle pan thathas an outlet edge located near a supply of absorbent core fibroussubstrate material that is moving in a machine direction. The supply ofparticulate matter passes over the outlet edge to exit the feed tray. Amechanism operates the shuttle pan through a range of motion having aforward stroke and a backward stroke. During the forward stroke, theoutlet edge follows the supply of absorbent core fibrous substratematerial.

[0019] In accordance with other features of preferred embodiments of theinvention, the particulate matter is a superabsorbent polymer, and theabsorbent core fibrous substrate material is a cellulose acetate tow.

[0020] In accordance with still other features of various embodiments ofthe invention, the feed tray may be a vibratory feed tray or a fixedfeed tray. In embodiments in which the feed tray is a fixed feed tray,the apparatus may further include a metered flow device for conveyingparticulate matter to the inlet of the feed tray.

[0021] In accordance with still other features of various embodiments ofthe invention, a loss-in-weight controller may be used to control theamount of particulate matter that is deposited onto the absorbent corefibrous substrate material.

[0022] In accordance with yet another embodiment of the invention, amethod for dry depositing zoned particulate matter onto a supply ofabsorbent core fibrous substrate material moving in a machine directionis provided. The method includes the steps of supplying particulatematter to a feed tray that has a shuttle pan and sliding the shuttle panthrough a range of motion having a forward stroke and a backward stroke.During the forward stroke an outlet edge of the shuttle pan follows thesupply of absorbent core fibrous substrate material, thereby depositingzones having a relatively high concentration of particulate matter ontothe absorbent core fibrous substrate material.

[0023] In accordance with other features of preferred embodiments of theinventive method, the particulate matter is a superabsorbent polymer,and the opened tow is a cellulose acetate tow.

[0024] In accordance with other features of various embodiments of theinventive method, the method further includes vibrating the feed tray,supplying particulate matter with a metered flow device, and controllingthe amount of particulate matter deposited using a loss-in-weightcontrol system.

[0025] These and other features of the invention will be readilyapparent from the Detailed Description that follows, along withreference to the drawings appended hereto.

BRIEF DESCRIPTION OF THE DRAWINGS

[0026]FIG. 1 is a plan view of a diaper-type absorbent garment, shownwith the effects of elastics removed for clarity;

[0027]FIG. 2 is a cross-sectional view of the garment of FIG. 1, asviewed from reference line AA;

[0028]FIG. 3 is a partially cut away side view of a system for dryforming absorbent cores and other structures and machinery according toa preferred embodiment of the present invention, shown in operation andin relation to a portion of an absorbent garment manufacturing line;

[0029]FIG. 4 is a partially cut away view of a feed tray according to apreferred embodiment of the present invention, shown at one end of itsrange of movement and showing the other end of its range of movement indashed lines;

[0030]FIG. 5A is a cut away view of a portion of a feed tray accordingto a preferred embodiment of the present invention;

[0031]FIG. 5B is a cut away view of a portion of another feed trayaccording to a preferred embodiment of the present invention;

[0032]FIG. 6 is a partially cut away side view of a feed tray, motor andside plates according to a preferred embodiment of the presentinvention;

[0033]FIG. 7 is an isometric view of the outlet portion of a feed trayaccording to a preferred embodiment of the present invention;

[0034]FIG. 8 is an isometric view of the outlet portion of a feed trayaccording to another embodiment of the present invention;

[0035]FIG. 9 is an isometric view of a combining drum according to apreferred embodiment of the present invention;

[0036]FIG. 10 is a sectional view of the vacuum surface of a combiningdrum according to a preferred embodiment of the present invention, shownoperating with the core composite adjacent the vacuum surface;

[0037]FIG. 11 is a partially exploded isometric view of anothercombining drum according to a preferred embodiment of the presentinvention;

[0038]FIG. 12 is an isometric view of yet another combining drumaccording to a preferred embodiment of the present invention;

[0039]FIG. 13 is a cross sectional view of a combining drum assemblyaccording to a preferred embodiment of the present invention as viewedfrom a direction orthogonal to the rotating axis of the combining drum,and as seen from reference line BB of FIG. 14;

[0040]FIG. 14 is a cross sectional view of the combining drum assemblyof FIG. 13, as seen from reference line AA;

[0041]FIG. 15 is a partially cut away view of the combining drumassembly of FIG. 13, shown with the outer drum partially removed;

[0042]FIG. 16 is a cross sectional view of a shuttle pan feed trayaccording to a preferred embodiment of the present invention;

[0043]FIG. 17 is a cross sectional view of another shuttle pan feed trayaccording to another preferred embodiment of the present invention;

[0044]FIG. 18A is an isometric view of a shuttle pan feed tray accordingto a preferred embodiment of the present invention shown in a firststage of operation;

[0045]FIG. 18B is an isometric view of the shuttle pan feed tray of FIG.18A shown in a second stage of operation;

[0046]FIG. 18C is an isometric view of the shuttle pan feed tray of FIG.18A shown in a third stage of operation;

[0047]FIG. 18D is an isometric view of the shuttle pan feed tray of FIG.18A shown in a fourth stage of operation;

[0048]FIG. 18E is an isometric view of the shuttle pan feed tray of FIG.18A shown in a fifth stage of operation;

[0049]FIG. 19 is a plot of a movement profile for the shuttle pan ofFIGS. 18A-18E; and,

[0050]FIG. 20 is an isometric view of a shuttle pan feed tray accordingto another preferred embodiment of the present invention having a fixedfeed tray and a metered flow device feeding the feed tray.

DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS

[0051] As used herein, the term “absorbent garment” or “garment” refersto garments that absorb and contain exudates, and more specifically,refers to garments that are placed against or in proximity to the bodyof the wearer to absorb and contain the various exudates discharged fromthe body. A non-exhaustive list of examples of absorbent garmentsincludes diapers, diaper covers, disposable diapers, training pants,feminine hygiene products and adult incontinence products. The termgarment includes all variations of absorbent garments, includingdisposable absorbent garments that are intended to be discarded orpartially discarded after a single use (i.e., they are not intended tobe laundered or otherwise restored or reused) and unitary disposableabsorbent garments that have essentially a single structure (i.e., donot require separate manipulative parts such as a diaper cover andinsert). As used herein, the term “diaper” refers to an absorbentgarment generally worn by infants and incontinent persons about thelower torso.

[0052] The claims are intended to cover all of the foregoing classes ofabsorbent garments, without limitation, whether disposable, unitary orotherwise. These classifications are used interchangeably throughout thespecification, but are not intended to limit the claimed invention. Theinvention will be understood to encompass, without limitation, allclasses of absorbent garments, including those described above.Preferably, the absorbent core is thin in order to improve the comfortand appearance of a garment. The importance of thin, comfortablegarments is disclosed, for example, in U.S. Pat. No. 5,098,423 toPieniak et al., which is incorporated herein by reference in itsentirety and in a manner consistent with the present invention.

[0053] Absorbent garments and diapers may have a number of differentconstructions. In each of these constructions it is generally the casethat an absorbent core is disposed between a liquid pervious,body-facing topsheet, and a liquid impervious, exterior facingbacksheet. In some cases, one or both of the topsheet and backsheet maybe shaped to form a pant-like garment. In other cases, the topsheet,backsheet and absorbent core may be formed as a discrete assembly thatis placed on a main chassis layer and the chassis layer is shaped toform a pant-like garment. The garment may be provided to the consumer inthe fully assembled pant-like shape, or may be partially pant-like andrequire the consumer to take the final steps necessary to form the finalpant-like shape. In the case of training pant-type garments and mostadult incontinent products, the garment is provided fully formed withfactory-made side seams and the garment is donned by pulling it up thewearer's legs. In the case of diapers, a caregiver usually wraps thediaper around the wearer's waist and joins the side seams manually byattaching one or more adhesive or mechanical tabs, thereby forming apant-like structure. For clarity, the present invention is describedherein only with reference to a diaper-type garment in which thetopsheet, backsheet and absorbent core are assembled into a structurethat forms a pant-like garment when secured on a wearer using fasteningdevices, although the invention may be used with other constructions.

[0054] Throughout this description, the expressions “upper layer,”“lower layer,” “above” and “below,” which refer to the variouscomponents included in the absorbent garments of the invention(including the layers surrounding the absorbent core units), as well asthe depiction in the drawings of certain layers or materials that are“above” or “below” one another, are used merely to describe the spatialrelationship between the respective components. The upper layer orcomponent “above” the other component need not always remain verticallyabove the core or component, and the lower layer or component “below”the other component need not always remain vertically below the core orcomponent. Indeed, embodiments of the invention include variousconfigurations whereby the core may be folded in such a manner that theupper layer ultimately becomes the vertically highest and verticallylowest layer at the same time. Other configurations are contemplatedwithin the context of the present invention.

[0055] The term “component” can refer, but is not limited, to designatedselected regions, such as edges, corners, sides or the like; structuralmembers, such as elastic strips, absorbent pads, stretchable layers orpanels, layers of material, or the like; or a graphic.

[0056] Throughout this description, the term “disposed” and theexpressions “disposed on,” “disposing on,” “disposed in,” “disposedbetween” and variations thereof (e.g., a description of the articlebeing “disposed” is interposed between the words “disposed” and “on”)are intended to mean that one element can be integral with anotherelement, or that one element can be a separate structure bonded to orplaced with or placed near another element. Thus, a component that is“disposed on” an element of the absorbent garment can be formed orapplied directly or indirectly to a surface of the element, formed orapplied between layers of a multiple layer element, formed or applied toa substrate that is placed with or near the element, formed or appliedwithin a layer of the element or another substrate, or other variationsor combinations thereof.

[0057] Throughout this description, the terms “top sheet” and “backsheet” denote the relationship of these materials or layers with respectto the absorbent core. It is understood that additional layers may bepresent between the absorbent core and the top sheet and back sheet, andthat additional layers and other materials may be present on the sideopposite the absorbent core from either the top sheet or the back sheet.

[0058] Throughout this description, the expression “fibrous material”denotes any fibrous material that may be used in an absorbent garment,including without limitation, various hardwood and softwood fluff pulps,tissues, cottons, and any other fibrous materials described herein.“Fibrous material” used in the context of the present invention is notintended to limit the invention to any particular type of fibrousmaterial.

[0059] Throughout this description, the expression “tow fibers” relatesin general to any continuous fiber. Tow fibers typically are used in themanufacture of staple fibers, and preferably are comprised of syntheticthermoplastic polymers. Usually, numerous filaments are produced by meltextrusion of the molten polymer through a multi-orifice spinneret duringmanufacture of staple fibers from synthetic thermoplastic polymers inorder that reasonably high productivity may be achieved. The groups offilaments from a plurality of spinnerets typically are combined into atow which is then subjected to a drawing operation to impart the desiredphysical properties to the filaments comprising the tow.

[0060] A preferred embodiment of the present invention comprises adisposable absorbent garment 10 of the diaper type, such as shown, forexample, in FIG. 1. It should be understood, however, that the presentinvention is applicable to other types of absorbent garments. Withreference to FIG. 1, the diaper 10 according to a first preferredembodiment is shown in a relaxed condition with the effects of theelastics removed for purposes of clarity in the description. The diaper10 has a generally hourglass shape and can generally be defined in termsof a front waist region 22, a back waist region 24, and a crotch region26. Those skilled in the art will recognize that “front” and “back” arerelative terms, and these regions may be transposed without departingfrom the scope of the present invention. Alternatively, the diaper canbe configured in a generally rectangular shape or in a “T” shape. A pairof leg openings 28 a, 28 b extend along at least a portion of the crotchregion 26. The diaper preferably comprises a topsheet 2, a backsheet 4,which may be substantially coterminous with the topsheet 2, and anabsorbent core 6 disposed between at least a portion of the topsheet 2and backsheet 4. One or more pairs of leg elastics 8 (three pairs areshown in FIG. 1) may be disposed to extend adjacent to leg openings 28a, 28 b, respectively. Of course, in other embodiments, the leg elastics8 may be omitted altogether.

[0061] The diaper may further include a front waist elastic system 30 a,a back waist elastic system 30 b, a fastening system 32 (e.g., tape orother suitable mechanical fastener) and a waste containment system inthe form of waste containment flaps 12 (also known as standing leggathers). Waste containment flaps 12 (FIG. 2) preferably extend from thefront waist region 22 to the back waist region 24 along opposite sidesof a longitudinal center line or axial center line 60 of the diaper 10,or alternatively only along a portion thereof. The front waist region 22and rear waist region 24 may include ear portions 38, 40 extendingoutwardly from the leg openings 28 a, 28 b.

[0062] A variety of backsheet and topsheet constructions and materialsare available and known in the art, and the invention is not intended tobe limited to any specific materials or constructions of thesecomponents. The backsheet 4 is of any suitable pliable liquid-imperviousmaterial known in the art. Typical backsheet materials include films ofpolyethylene, polypropylene, polyester, nylon, and polyvinyl chlorideand blends of these materials. For example, the backsheet can be apigmented polyethylene film having a thickness in the range of 0.02-0.04mm. The moisture-pervious topsheet 2 can be any suitable relativelyliquid-pervious material known in the art that permits passage of liquidtherethrough. Non-woven topsheet materials are exemplary because suchmaterials readily allow the passage of liquids to the underlyingabsorbent core 6. Examples of suitable topsheet materials includenon-woven spunbond or carded webs of polypropylene, polyethylene, nylon,polyester and blends of these materials.

[0063] The backsheet 4 and the topsheet 2 preferably are “associated”with one another. The term “associated” encompasses configurationswhereby the topsheet 2 is directly joined to the backsheet 4 by affixingthe topsheet 2 directly to the backsheet 4, and configurations wherebythe topsheet 2 is indirectly joined to the backsheet 4 by affixing thetopsheet 2 to intermediate members which in turn are affixed to thebacksheet 4. While the backsheet 4 and topsheet 2 in the preferredembodiment have substantially the same dimensions, they may also havedifferent dimensions.

[0064] In addition, the backsheet 4 may be covered with a fibrous,nonwoven fabric such as is disclosed for example in U.S. Pat. No.4,646,362, which is incorporated herein by reference in its entirety andin a manner consistent with the present invention. Materials for such afibrous outer liner include a spun-bonded nonwoven web of syntheticfibers such as polypropylene, polyethylene or polyester fibers; anonwoven web of cellulostic fibers, textile fibers such as rayon fibers,cotton and the like, or a blend of cellulostic and textile fibers; aspun-bonded nonwoven web of synthetic fibers such as polypropylene;polyethylene or polyester fibers mixed with cellulostic, pulp fibers, ortextile fibers; or melt blown thermoplastic fibers, such as macro fibersor micro fibers of polypropylene, polyethylene, polyester or otherthermoplastic materials or mixtures of such thermoplastic macro fibersor micro fibers with cellulostic, pulp or textile fibers.

[0065] The backsheet 4 may comprise multiple panels, such as threepanels wherein a central poly backsheet panel is positioned adjacent theabsorbent core while outboard non-woven breathable side backsheet panelsare attached to the side edges of the central poly backsheet panel. Thebacksheet may also be formed from microporous poly coverstock for addedbreathability. In other embodiments, the backsheet may be a laminate ofseveral sheets. The backsheet may further be treated to render ithydrophilic or hydrophobic, and may have one or more visual indicatorsassociated with it, such as labels indicating the front or back of thediaper or other characters or colorations. The present invention is notlimited to any particular backsheet 4 material or construction.

[0066] The topsheet 2 may be formed from one or more panels of materialand may comprise a laminated sheet construction. In the embodiment ofFIG. 1, the topsheet comprises three separate portions or panels. Athree-panel topsheet may comprise a central topsheet panel 2 a (FIG. 2)that preferably is formed from a liquid-pervious material that is eitherhydrophobic or hydrophilic. The central topsheet panel 2 a may be madefrom any number of materials, including synthetic fibers (e.g.,polypropylene or polyester fibers), natural fibers (e.g., wood orcellulose), apertured plastic films, reticulated foams and porous foamsto name a few. One preferred material for a central topsheet panel 2 ais a cover stock of single ply non-woven material which may be made ofcarded fibers, either adhesively or thermally bonded, perforated plasticfilm, spunbonded fibers, or water entangled fibers, which generallyweigh from 0.3-0.7 oz./yd² and have appropriate and effective machinedirection and cross-machine direction strength suitable for use as ababy diaper cover stock material, as are known in the art. The centraltopsheet panel 2 a preferably extends from substantially the front waistregion 22 to the back waist region 24 or a portion thereof.

[0067] The second and third topsheet panels 2 b, 2 c in this embodimentmay be positioned laterally outside of the central topsheet panel 2 a.The outer topsheet panels 2 b, 2 c preferably are substantiallyliquid-impervious and hydrophobic, preferably at least in the crotcharea. The outer edges of the outer topsheet panels may substantiallyfollow the corresponding outer perimeter of the backsheet 4. Thematerial for the outer topsheet portions or panels preferably ispolypropylene and can be woven, non-woven, spunbonded, carded or thelike, depending on the application.

[0068] An inner region 34 (FIG. 2) of the outer topsheet portions orpanels 2 b, 2 c preferably is attached by, e.g., an adhesive, to theouter edges 36 of the inner topsheet portion or panel 2 a. At the pointof connection with the outer edges 36 of the inner topsheet portion orpanel 2 a, the inner regions 34 of the outer topsheet portions or panels2 b, 2 c extend upwardly to form waste containment flaps 12. The wastecontainment flaps 12 may be formed of the same material as the outertopsheet portions or panels 2 b, 2 c, as in the embodiment shown. Thewaste containment flaps 12 may also be formed from separate elasticizedstrips of material that are associated with the topsheet, backsheet orboth, or otherwise integrated into the garment.

[0069] The waste containment flaps 12 may be treated with a suitablesurfactant to modify their hydrophobicity/hydrophilicity or imbue themwith skin wellness products as desired. The central topsheet portion orpanel 2 a may extend past the connection point with the wastecontainment flaps 12 and even extend to the periphery of the backsheet.Still further, the central topsheet portion or panel 2 a could extendfully between the outer topsheet portions or panels 2 b, 2 c and evenbeyond so that the outer edges 36 of the central topsheet portion orpanel 2 a are coextensive with and sandwiched between the outer topsheetportions or panels 2 b, 2 c and the backsheet 4.

[0070] The waste containment flaps 12 each preferably includes a portionthat folds over onto itself to form an enclosure. One or more elasticmembers 14 (FIG. 2) may be secured in the enclosure in a stretchedcondition. As has been known at least as long the disclosure ofTetsujiro, Japanese Patent document 40-11543, when the flap elastic 14attempts to assume the relaxed, unstretched condition, the wastecontainment flaps 12 rise above the surface of the central topsheetportion or panel 2 a. Various other configurations of topsheets 2 andwaste containment systems, such as flaps 12, are known in the art, andthe present invention is not intended to be limited to any particulardesign for these components.

[0071] The waist elastics 30 a, 30 b (FIG. 1) may be similar structuresor different to impart similar or different elastic characteristics tothe front and back waist portions 22, 24 of the diaper. In general, thewaist elastics may comprise elastically extensible foam stripspositioned at the front and back waist sections 22, 24. The foam stripsare preferably about 0.50 inches to about 1.50 inches wide and about 3inches to about 6 inches long. The foam strips are preferably positionedbetween the topsheet portions or panels and the backsheet 4.Alternatively, a plurality of elastic strands may be employed as waistelastics rather than foam strips. The foam strips are preferablypolyurethane, but could be any other suitable material that preferablydecreases waist band roll over, reduces leakage over the waist ends ofthe absorbent garment, and generally improves comfort and fit. The frontand back waist foam strips 30 a, 30 b are stretched 50-150%, preferably100% before being adhesively secured between the backsheet 4 andtopsheet 2. Waist elastics are known in the art, and the presentinvention is not limited to the use of a particular waist elasticsystem, or to the inclusion of waist elastics at all.

[0072] Each leg opening 28 a, 28 b may be provided with a leg elasticcontainment system 8, sometimes referred to as conventional leg gathers.In a preferred embodiment, three strands of elastic threads arepositioned to extend adjacent the leg openings 28 a, 28 b between theouter topsheet portions or panels 2 b, 2 c and the backsheet 4. theselection of appropriate elastics and the construction of leg elasticcontainment systems is known in the art. For example, the leg elastics 8may be ultrasonically bonded, heat/pressure sealed using a variety ofbonding patterns, or glued to the diaper 10.

[0073] Various commercially available materials may be used for the legelastics 8 and elastic members 14, such as natural rubber, butyl rubberor other synthetic rubber, urethane, elastomeric materials such asspandex, which is marketed under various names, including LYCRA(DuPont), GLOSPAN (Globe) and SYSTEM 7000 (Fulflex), and so on. Thepresent invention is not limited to any particular elastic.

[0074] The fastening system of the diaper 10 may be attached to the backwaist region 24, and preferably comprises tape tabs or mechanicalfasteners 32. However, any fastening known in the art will beacceptable. Moreover, the fastening system may include a reinforcementpatch below the front waist portion so that the diaper may be checkedfor soiling without compromising the ability to reuse the fastener.Alternatively, other diaper fastening systems are also possible,including safety pins, buttons, and snaps. Fastening systems are knownin the art, and the present invention is not limited to using anyparticular fastening, and may be constructed without any fasteningsystem at all, such as in training pant-type garments.

[0075] As stated previously, the invention has been described inconnection with a diaper. The invention, however, is not intended to belimited to application only in diapers. Specifically, the presentinvention may be readily adapted for use in other absorbent garmentsbesides diapers, including, but not limited to, training pants, femininehygiene products and adult incontinence products.

[0076] The underlying structure beneath the topsheet 2 may include,depending on the diaper construction, various combinations of elements,but in each embodiment, it is contemplated that the absorbent garmentwill preferably include an absorbent core 6. For example, an additionallayer 20 may be disposed between the topsheet 2 and absorbent core 6, asshown in FIG. 2, and/or other additional layers may be disposed betweenthese layers, or between absorbent core 6 and backsheet 4. Theadditional layer 20 or layers may comprise any useful layer known in theart or developed hereafter, such as a fluid acquisition layer, adistribution layer, an additional fibrous layer optionally containingSAP, a wicking layer, a storage layer, or combinations and fragments ofthese layers. Such layers may be provided to assist with transferringfluids to the absorbent core 6, handling fluid surges, preventing rewet,containing absorbent material, improving core stability, or for otherpurposes. Skilled artisans are familiar with the various additionallayers that may be included in absorbent article, and the presentinvention is not intended to be limited to any particular type ofmaterials used for those layers. Rather, the invention encompasses alltypes of wicking layers, all types of distribution layers, etc., to theextent that type of layer 20 is utilized.

[0077] The dimensions of additional layer(s) 20 may be the same as ordifferent from the dimensions of the absorbent core 6 and/or topsheet 2and backsheet 4. It is preferred that additional layer(s) 20 have awidth in the lateral direction (102) of anywhere from about 10 mm toabout 100 mm, and preferably from about 25 mm to about 80 mm.

[0078] Although the absorbent core 6 depicted in FIG. 1 has asubstantially rectangular shape as viewed in the plan view, other shapesmay be used, such as a “T” shape or an hourglass shape. The absorbentcore 6 may extend into either or both of the front and back waistregions 24, 22. The shape and construction of the absorbent core 6 maybe selected to provide the greatest absorbency in target areas wherebody fluids are most likely to strike the diaper 10, which is oftenreferred to as zoned absorbency. The absorbent core 6 may also comprisea number of layers of similar or different construction. The absorbentcore may be associated with the topsheet 2, backsheet 4, or any othersuitable part of the garment 10 by any method known in the art, in orderto fix the absorbent core 6 in place.

[0079] Generally, in a preferred embodiment, the absorbent core 6comprises particles of super absorbent polymer distributed within afibrous structure. Additional fibrous or particulate additives may bedisposed within the absorbent core 6 to add to the core's strength andSAP efficiency or to otherwise enhance the performance of the garment.The absorbent core 6 may be partially or wholly surrounded by a tissuelayer 16, 18, and other additional layers 20 may be added to providefurther benefits. The various components of the absorbent core 6 are nowdescribed in greater detail.

[0080] Certain fibrous materials preferably are used to form the fibrousstructure of the absorbent core 6 of the present invention. Thesefibrous materials maintain high SAP efficiencies when the SAPconcentration is in the range of about 50-95%, more preferably about60-90%, and most preferably about 75-85%. For example, the fibrousstructure of the absorbent core 6 may be made with cellulose acetatefibers, rayon fibers, Courtauld's LYOCELL fibers, polyacrylonitrilefibers, surface-modified (hydrophilic) polyester fibers,surface-modified polyolefin/polyester bicomponent fibers,surface-modified polyester/polyester bicomponent fibers, cotton fibers,blends of the foregoing materials, and the like.

[0081] Of the foregoing, cellulose acetate tow fibers are the mostpreferred materials for use as the fibrous structure. In addition,rayon, Courtauld's LYOCELL, polyacrylonitrile, cotton fibers and cottonlinters have similar properties to cellulose acetate and arealternatively preferred. The remaining fibers, surface-modifiedpolyolefin/polyester bicomponent fibers, and surface-modifiedpolyester/polyester bicomponent fibers are also believed to be effectiveas a fibrous structure or as fibrous additives. To maintain high SAPconcentrations, the weight concentration of fibrous material forming theabsorbent core 6 of the invention preferably is about 5-50%, morepreferably about 10-30%, and most preferably about 15-25%. Mostpreferably, the absorbent core 6 comprises from about 75-85% SAP andfrom about 15-25% fibrous structure material chosen from the foregoinggroup.

[0082] In accordance with the present invention, improved absorbentarticles are advantageously based upon continuous crimped filament tow,and accordingly, the central fibrous structure of the core 6 isadvantageously prepared therefrom. This fiber structure has highstructural integrity, and as such, is distinct from a matrix ofdiscontinuous fibers, often described as fluff or fluff pulp, that iscommonly used in the prior art. The high structural integrity enablesthe production of stronger webs than those formed from discontinuousfibers, which in turn are believed to enable the production of thinnerabsorbent pads. In addition, the use of such fibers enables theproduction of ultra low density absorbent cores, when compared toabsorbent cores prepared by dispersing SAP particles in fluff. Thereduction in density is largely attributable to the reduced weight ofthe fibrous structure. Absorbent cores 6 constructed from a blend ofsuch materials and SAP are referred to herein as “tow/SAP” cores or“tow-based” cores.

[0083] Beneficially, cellulose ester tow is used to form the fibrousstructure. Non-limiting examples of suitable cellulose esters includecellulose acetate, cellulose propionate, cellulose butyrate, cellulosecaproate, cellulose caprylate, cellulose stearate, highly acetylatedderivatives thereof such as cellulose diacetate, cellulose triacetateand cellulose tricaproate, and mixtures thereof such as celluloseacetate butyrate. A suitable cellulose ester will include the ability toabsorb moisture, preferably is biodegradable, and is influenced not onlyby the substituent groups but also by the degree of substitution. Therelationship between substituent groups, degree of substitution andbiodegradability is discussed in W. G. Glasser et al, BIOTECHNOLOGYPROGRESS, vol. 10, pp. 214-219 (1994), the disclosure of which isincorporated herein by reference in its entirety.

[0084] Continuous filament tow useful in the present invention isbeneficially moisture-absorbent and biodegradable. Accordingly,cellulose acetate tow typically is preferred for use in the invention.Typically, the denier per fiber (dpf) of the tow fiber will be in therange of about 1 to 9, preferably about 3 to 6, and most preferablyabout 4. For the same weight product, filaments of lower dpf may provideincreased surface area and increased moisture absorption. Total denierof the tow may vary within the range of about 20,000 to 60,000,depending upon the process used, and is preferably about 35,000. Thefibers may have a circular, ovate, rectilinear, or any other crosssection. In one embodiment, the fibers have a tri-lobal cross sectionwith an area of about 3.36×10⁻⁶ cm². Such a cross-sectional shape mayprovide improved bending stiffness, increased wicking, or otherbeneficial properties.

[0085] Tow typically is provided as a relatively dense matrix of fibers,and it is often desirable to “open” (also known as “fluffing” or“blooming”) the tow into a more voluminous cotton-like matrix. To thisend, it is particularly preferred in the invention to use tow havingcrimped filaments, as the crimps aid with opening the tow. Theseparation of filaments resulting from the opening processadvantageously results in increased available filament surface area forsuperabsorbent material immobilization and increased moistureabsorption. Gel blocking also may be reduced by using crimped tow in theabsorbent core 6. As therefore may be understood, more crimp istypically better, with an excess of about 20 crimps per inch beingusually preferred. Continuous filament cellulose ester tow havingcrimped filaments with about 25 to 40 crimps per inch is commerciallyavailable from Hoechst Celanese Corporation of Charlotte, N.C.

[0086] If desired, an absorbent core 6 of multiple layer thickness maybe provided. To this end, the tow may be, for example, lapped orcrosslapped in accordance with conventional procedures. In this way, asuperabsorbent, absorptive material of a desired weight and/or thicknessmay be provided. The specific weight or thickness will depend uponfactors including the particular end use.

[0087] Any superabsorbent polymer (SAP) now known or later discoveredmay be used in the absorbent core 6, so long as it is capable ofabsorbing liquids. Useful SAP materials are those that generally arewater-insoluble but water-swellable polymeric substances capable ofabsorbing water in an amount that is at least ten times the weight ofthe substance in its dry form. In one type of SAP, the particles orfibers may be described chemically as having a back bone of natural orsynthetic polymers with hydrophilic groups or polymers containinghydrophilic groups being chemically bonded to the back bone or inintimate admixture therewith. Included in this class of materials aresuch modified polymers as sodium neutralized cross-linked polyacrylatesand polysaccharides including, for example, cellulose and starch andregenerated cellulose which are modified to be carboxylated,phosphonoalkylated, sulphoxylated or phosphorylated, causing the SAP tobe highly hydrophilic. Also included are water swellable polymers ofwater soluble acrylic or vinyl monomers crosslinked with apolyfunctional reactant. Such modified polymers may also be cross-linkedto reduce their water-solubility, and such cross-linked SAPs have beenfound to provide superior performance in some absorbent cores. A moredetailed recitation of superabsorbent polymers is found in U.S. Pat. No.4,990,541 to Nielsen, the disclosure of which is incorporated herein byreference in its entirety. The SAP is preferable selected to providehigh absorbency performance for the particular application. The measureof the SAP's absorbency performance may be evaluated in a number ofways, as will be understood by those skilled in the art. For example, itmay be desirable to provide a SAP having a high measure of saline flowconductivity (SFC), as is described in U.S. Pat. No. 5,562,646 toGoldman et. al, which is incorporated herein by reference in itsentirety and in a manner consistent with the present invention. Ofcourse, the SAP may be selected to provide other properties orcombinations of properties as well.

[0088] Commercially available SAPs include a starch modifiedsuperabsorbent polymer available under the trade name SANWET® fromHoechst Celanese Corporation, Portsmouth, Va. SANWET® is a starchgrafted polyacrylate sodium salt. Other commercially available SAPsinclude a superabsorbent derived from polypropenoic acid, availableunder the trade name DRYTECH® 520 SUPERABSORBENT POLYMER from The DowChemical Company, Midland Mich.; AQUA KEEP manufactured by SeitetsuKagaku Co., Ltd.; ARASORB manufactured by Arakawa Chemical (U.S.A.)Inc.; ARIDALL 1125 manufactured by Chemdall Corporation; and FAVORmanufactured by Stockhausen Inc. Still other commercially available SAPsinclude SA55SX, avalable from Sumitomo Chemical Co. Ltd. of Osaka,Japan, and T7700 and T7200 provided by BASF of Mount Olive, N.J.

[0089] The SAP may be provided in any particle size, and suitableparticle sizes vary greatly depending on the ultimate propertiesdesired. Preferably, a fine particulate rather than a coarseparticulate, is used in the invention, and preferably a fine particulatethat passes through an about 200 mesh screen is used.

[0090] It has been known to prepare absorbent cores comprised ofcellulose acetate tow or other polymeric fibers and SAP, as described inU.S. Statutory Invention Registration H1565, and U.S. Pat. Nos.5,436,066, and 5,350,370, the disclosures of each of which areincorporated by reference herein in their entirety and in a mannerconsistent with the present invention. It was conventional to addtackifying agents, specific size fibers, or specific fibers incombination with fluff, in order to prepare the absorbent core andimmobilize the SAP particles. These additional materials may add todensity of the core, or otherwise adversely affect the overallperformance of the absorbent garment made therefrom. Thus, it ispreferred not to use ethylene glycol, tackifying agents, and very smallparticulate fibers in the invention, although they may be used to theextent they do not reduce the overall performance of the garment.

[0091] The total basis weights of the absorbent core 6 including fibrousmaterials, SAP, tissue, additional layers, and additives, are anywherefrom about 100 grams per square meter (gsm) to about 1,000 gsm. The mostpreferred total basis weights of the absorbent core 6 are about 500 gsmto about 700 gsm.

[0092] Additional particles or fibrous additives may be added to theabsorbent core 6 to help maintain high SAP efficiency, to reduce thecost of the garment, or to provide other benefits. Fibrous additives maybe introduced as part of the supply of unopened fibers, preferably towfibers, or may be added to the fibers, preferably tow fibers, after ithas been opened. In a preferred embodiment, particulate additivesgenerally may be added to the tow after it has been opened to allowpractical manufacture of the tow and to prevent losses of theparticulate additives during processing.

[0093] In one embodiment, about 1-10%, and preferably about 5%, byweight of thermally bondable synthetic fibers may be added to theabsorbent core 6 to impart additional wet strength to the laminate.These additive fibers may improve the stability of the core during useof the diaper. The preferred synthetic fibers for such an embodiment arepolyolefin/polyester fibers and polyester/polyester bicomponent fibers.

[0094] In another embodiment, the fibrous structure may comprise acombination of preferred tow materials, such as a blend of celluloseester and conventional soft or hard wood fibers. Such combinations maybe useful to maintain the improved SAP efficiency available from thecrimped filament tow-based fibrous structure while providing additionalbenefits. For example, it has been discovered that an absorbent core 6having a 150 g/m² composite comprised of 80% SAP, 10% cellulose acetate,and 10% conventional fluff pulp has a SAP efficiency of about 85%,whereas an absorbent core 6 comprised of 80% SAP and 20% fluff pulp SAPhas an efficiency of about 70%.

[0095] The particulate additives that may be added to the absorbent core6 preferably are insoluble, hydrophilic polymers with particle diametersof 100 μm or less. These particulate additives may be chosen to impartoptimal separation of the SAP particles. Examples of preferredparticulate additive materials include, but are not limited to, potato,corn, wheat, and rice starches. Partially cooked or chemically modified(i.e., modifying hydrophobicity, hydrophilicity, softness, and hardness)starches can also be effective. Most preferably, the particulateadditives comprise partially cooked corn or wheat starch because in thisstate, the corn or wheat are rendered larger than uncooked starch andeven in the cooked state remain harder than even swollen SAP. In anyevent, regardless of the particulate additive chosen, one of the manyimportant criteria is to use particulate additives that are hardhydrophilic materials relative to swollen SAP or which are organic orinorganic polymeric materials about 100 microns in diameter. Fibrous andparticulate additives can be used together in these absorbent laminates.Examples of SAP/particulate and SAP/fiber/particulate additives includethose described in, for example, U.S. Pat. No. 6,068,620.

[0096] Other particulate or powdered additives also may be depositedwithin the absorbent core 6 to provide odor control, skin wellness, andimproved appearance. For example, zeolites, sodium bicarbonate andperfumes may be added to reduce or mask odors, and titanium dioxide orother color-imbuing compounds may be added to provide the absorbent core6 with a more pleasant color.

[0097] The absorbent core 6 preferably comprises a tissue wrapping thatat least partially encloses the preferred blended tow and SAP, such asdisclosed in U.S. Pat. No. 6,068,620. The tissue wrapping is useful, forexample, for containing the SAP within the absorbent core 6 andproviding strength to the core during manufacturing and use. In apreferred embodiment, the tissue wrapping comprises first and secondtissue layers 16, 18 that encase the absorbent core 6, and mayoptionally also encase one or more additional layers 20. Preferably, thefirst tissue layer 16 is located generally between the topsheet 2 andthe absorbent core 6, and is hydrophilic and fluid pervious. It is alsopreferred that the second tissue layer 18 be located between thebacksheet 4 and the absorbent core 6 and be hydrophobic and fluidimpervious. The tissue wrapping may also comprise a single tissue layerthat has been folded to encase the absorbent core, and that may be zonetreated to render the portion that forms the lower tissue layer 18hydrophobic and fluid impervious. The tissue layers 16, 18 or the wholecore 6 may be crimped, folded, sealed or bonded to help contain the SAPparticles.

[0098] In one embodiment, the fibrous structure and SAP of the absorbentcore may be adhesively or thermally bonded to improve the absorbentcore's wet strength and core stability. This, unfortunately, may resultin slower than adequate rates of absorption and poor SAP efficiency. Inanother embodiment the SAP and fibrous structure may be hydrogen bondedto additional the tissue layers 16, 18. When a tow-based fibrousstructure having a high concentration of SAP is hydrogen bonded to firstand second tissue layers 16, 18 to form an absorbent core 6, the SAPefficiency is not impaired, wet strength increases, and the first andsecond tissue layers 16, 18 add stability to the core 6 duringmanufacture. It has been found that when the fibrous structure of theabsorbent core 6 is hydrogen bonded using water to the tissue layers 16,18, unexpectedly good “core utilization” is realized. “Core utilization”is the percentage of the total capacity of a core that can be absorbedin a demand absorbency test. This unexpected performance improvement isbelieved to be the result of the beneficial liquid distribution providedby the intimate bond between the fibers of the fibrous structure and thetissue layers 16, 18.

[0099] In another preferred embodiment, the first and second tissuelayers 16, 18 are coated with adhesive prior to being placed on eitherside of the absorbent core 6, thereby providing strength to the core andadhesively holding a portion of the SAP in place during use. The tissuelayers 16, 18 may be provided having a width greater than the fibrousstructure of the absorbent core 6, and the portions of the tissue layers16, 18 extending past either side of the fibrous structure of the core 6may be bonded to one another to provide further SAP retentioncapability. In still another embodiment, if the fibrous structurecontains about 1-5% by weight thermally bondable synthetic fibers,bonding to the tissue layers 16, 18 may be achieved using thermal bonds.

[0100] The absorbent core 6 of the present invention may flat or foldedwhen it is fixed in place between the topsheet 2 and backsheet 4. Foldedcores may provide additional performance benefits, such as improvedfluid redistribution, greater SAP efficiency, and so on. The absorbentcore 6 can be folded in any suitable manner, including any and all ofthose disclosed in U.S. Pat. No. 6,068,620. Those skilled in the artwill appreciate that the absorbent core 6 can be folded such that theadjacent sides are touching one another, or so that channels are formedin certain areas. For example, the absorbent core 6 can be folded in theform of a “C” where the curled ends may be spaced apart to form achannel there between, and the lower edges of the curled ends may bedisposed adjacent the upper edges of the bottom portion of the foldedarticle. Alternatively, another absorbent material, or another absorbentcore 6 may be disposed in the space formed by the standard “C” fold. Thesame considerations may be given to embodiments having a “G” fold or a“U” fold where the spaces formed by these folds may be filled withanother absorbent material, another absorbent core 6, left open to formfluid handling channels, or the folds may be made tight enough so thatlittle or no space is formed. Other possible arrangements include a “Z”fold, and a pleated absorbent core 6, and other folded shapes, as willbe appreciated by those skilled in the art.

[0101] The absorbent core 6 preferably is formed using a dry process.Dry processes have numerous benefits over wet processes. For example, inwet processes, the core material is typically immersed in a fluid havinga superabsorbent particles mixed or suspended therein, and the corematerial may require additional drying steps and other steps that add tothe complexity and cost of the core forming process. In addition, wetprocesses often require the absorbent core to be manufactured off of themain assembly line. Dry processes typically have lower operating coststhan wet processes because the equipment used in dry processes istypically less complex and can run at higher line speeds. Further, dryforming processes may often be adapted for use directly on the line ofconventional diaper machines. A preferred embodiment of the presentinvention is particularly concerned with using a dry forming process tomanufacture absorbent cores having high concentrations of SAP andrelatively low basis weights, while overcoming or avoiding thedeficiencies of known dry forming processes and machines, as describedelsewhere herein.

[0102] One challenge with making absorbent cores having highconcentrations of SAP and relatively low basis weight fibrousstructures, as described above, is to achieve the desired distributionof SAP within the core. In many cases it may be desirable to achieve auniform distribution of SAP within the core to provide the absorbentgarment with uniform absorption capability. In such a case, not onlyshould the SAP be evenly distributed along the length and width of theabsorbent core, but it also should be properly distributed throughoutthe thickness of the core to ensure that the SAP is not subject to gelblocking or other inefficiencies during use. It also is desirable toprovide a controlled amount of SAP to the core to prevent overuse of theSAP, which typically is relatively expensive. It may be furtherdesirable to precisely control the distribution of SAP to provide localregions of the core that have greater SAP concentrations than others toprovide zoned absorbency. Such concentrations may be along one or moreof the absorbent core's length, width and thickness.

[0103] Referring now to FIG. 3, a preferred embodiment of an apparatusand method for dry forming composite cores is shown. In the preferredembodiment, a tow supply 302, which may be unopened or partially opened,is provided along a first path to enter a forming jet assembly 304. Thesupply of tow may comprise any material that is desired to be used asthe fibrous structure of the garment's absorbent core 6 and is suitablefor use in the process described herein, such as those that have beendescribed elsewhere herein. Those skilled in the art will appreciatethat if fibers, fluff, or pulp other than tow fibers are used, formingjet assembly 304 would be replaced by a suitable fiber or fluff formingapparatus, as are well known in the art. A preferred material for thetow supply 302 is a supply of cellulose acetate having a basis weight ofabout 50 g/m² to about 100 g/m², and more preferably of about 76 g/m².The tension, speed and path of the tow supply 302 may be adjusted by oneor more movable pulleys 306, guides (not shown) and/or festoons (notshown), as are known in the art.

[0104] The tow supply 302 enters the forming jet assembly 304 and isopened in preparation for being incorporated into absorbent cores. Theforming jet assembly 304 comprises a tow inlet 308 at one end into whichthe tow supply 302 is fed. One or more high velocity jets 310 of air orother gas are projected into the forming jet assembly to impinge uponthe tow supply 302 to thereby separate the fibers and “bloom” or openthe tow. Preferably, two jets 310 are used and each jet 310 is locatedproximal to the tow inlet 308 and on opposite sides of the tow supply302. Each of the jets 310 preferably comprises a flow of air moving atabout 17.5 cubic feet per minute through a slit-shaped port that has alength of about 3.94 inches and a width of about 0.003 inches. Similardevices for opening tow are known in the art, and disclosed, forexample, in U.S. Pat. No. 5,331,976 to St. Pierre, which is incorporatedherein by reference in its entirety and in a manner consistent with thepresent invention. Other devices and procedures for opening the towsupply 302 may also be used with the present invention, as will beunderstood by those skilled in the art.

[0105] The opened or “bloomed” tow 312 accumulates within the formingjet assembly 304 as it is being used, and the amount of opened tow 312being consumed may be measured by a level meter 314 (also known as a“dancer”). The level meter 314 may be any suitable electromechanical,optical, or other type of device capable of measuring the amount ofopened tow 312 being consumed. In a preferred embodiment, the levelmeter 314 is a plate that is pivotally attached to a rotary positionsensor (such as a commonly known variable resistance or potentialdevice). As the level of opened tow 312 increases or decreases, theplate pivots up and down, thereby changing the output of the rotaryposition sensor. In a preferred embodiment, the level meter 314 is usedas part of a closed-loop feedback algorithm or an open-loop algorithm tometer the rate at which the tow supply 302 is fed into the forming jetassembly 304, and may be integrated into a control system 320.

[0106] The control system 320 may comprise any electrical controlapparatus that may be configured to control one or more variables basedon the measurement of one or more inputs. Although the control system320 is referred to herein in the singular, it should be understood thata number of independent control systems 320 may be used for variousparts of the machinery, and these various systems are referred tocollectively herein as a single control system 320. The control system320 may control any number of variables and have any number of inputs,and may use an open-loop or closed-loop algorithm. Exemplary controlsystems 320 include programmable logic control (PLC) devices havingeasily used human machine interfaces, as are known in the art. Ofcourse, the control system 320 may simply comprise a human operator thatmonitors the various inputs and adjusts the various system variables.

[0107] The opened tow 312 preferably is pulled out of the forming jetassembly 304 by a vacuum draw roll 322, such as the combining drum 800described elsewhere herein in conjunction with FIG. 8, or a similardrawing device. The opened tow 312 exits the forming jet assembly 304 ata tow break angle Θ_(B), which may be adjusted by altering the positionof the vacuum draw roll 322 (or similar device), or, more preferably, byadjusting the height and angle of the forming jet assembly 304 usingadjustable mounts 324. Increasing the tow break angle Θ_(B) increasesthe drag on the opened tow 312 and thereby increases the amount ofstretch that the vacuum draw roll 322 imparts on the opened tow 312.Greater stretch reduces the basis weight of the opened tow 312 that ispulled onto the vacuum draw roll 322. The tow forming jet 304 preferablyis aligned so that its outlet is tangential to the vacuum draw roll 322or slightly above a tangent to the vacuum draw roll 322. In a preferredembodiment, the outlet of the tow forming jet 304 is located at atangent to the vacuum draw roll 322 to about 1 inch above a tangent tothe vacuum draw roll 322. In a more preferred embodiment the outlet ofthe tow forming jet 304 is less than about 0.75 inches above a tangentto the vacuum draw roll 322, and in a most preferred embodiment, theoutlet of the tow forming jet 304 is located less than about 0.5 inchesabove a tangent to the vacuum draw roll 322.

[0108] The tow forming jet's adjustable mounts 324 may be fixed in adesired position during machine operation, or may be actively operatedby a control system 320 during operation in response to measurements ofthe core basis weight or other feedback gathered during operation.Mechanical, electromechanical, pneumatic, hydraulic, or other suitableadjusting devices may be used to actuate the adjustable mounts 324, suchas stepper motors, solenoids and hydraulic or pneumatic pistons or rams,and the like. Alternatively, or in addition, the basis weight of theopened tow 312 may be adjusted by increasing or decreasing the speed ofthe vacuum draw roll 322, with faster speeds generally resulting in alower basis weight of the opened tow 312.

[0109] After the opened tow 312 exits the forming jet assembly 304, asupply of superabsorbent particles 326 is delivered to the opened tow312, and the tow/SAP composite is encased between first and secondcasing sheet supplies 316, 318. Alternatively, the tow/SAP composite maybe encased within a fold in a single casing sheet. Preferably, as shownin FIG. 3, the opened tow 312 is laid onto a first casing sheet supply316 before the SAP 326 is fed to the opened tow 312 to help contain theSAP 326 and control the SAP distribution, then the second casing sheetsupply 318 is laid on the tow/SAP composite to form an absorbent coresubassembly that may be processed into absorbent garments.

[0110] The first and second casing sheet supplies 316, 318 encase theopened tow and SAP composite. The first and second casing sheet supplies316, 318 preferably form the first and second tissue layers 16, 18 ofthe completed garment, but may also form the topsheet 2 and backsheet 4of the absorbent garment 10, or any other layers. The first and secondcasing sheet supplies 316, 318 are preferably wider than the opened tow312 that forms the absorbent core 6, and their side portions arepreferably sealed to one another by bonding or crimping to preventrelease of opened tow 312 and particles of SAP. The absorbent corecomposite 348, comprising the assembly of the first and second casingsheet supplies 316, 318 and the opened tow 312 and SAP 326 core, may befurther processed as it is conveyed through the assembly line forinclusion into absorbent garments 10. For example, in a preferredembodiment, the absorbent core composite 348 is severed into individualabsorbent cores 6, and the severed ends may be crimped or bonded toprevent the SAP 326 from exiting the ends.

[0111] In all cases, at least one of the first and second casing sheets316, 318 should be liquid permeable and positioned in the garment toface the wearer's body to allow the flow of fluids into the core 6. Theother casing sheet supply may optionally be liquid impermeable. Theliquid impermeability or permeability of either of the casing sheetsupplies 316, 318 may be provided by chemical or physical treatment, orby the proper selection of materials, as is known in the art. In analternative preferred embodiment, the first and second casing sheets316, 318 may both be formed from a single sheet of material that isfolded to encase the opened tow 312 and SAP 326.

[0112] It may be desirable to apply an adhesive to one or both of thefirst and second casing sheet supplies 316, 318 prior joining them withthe opened tow 312 or tow/SAP combination. For example, in one preferredembodiment, an adhesive is applied to the entire width of one or both ofthe casing sheet supplies 316, 318 by adhesive applicators 328 beforethey are joined with the opened tow 312 to provide a better bond betweenthe casing sheets 316, 318 and the tow/SAP composite. In such anembodiment, the adhesive may also function to fix a portion of the SAPparticles 326 in place. In another preferred embodiment, the suppliescasing sheet material 316, 318 are wider than the tow/SAP composite, andadhesive is applied along the lateral edges of one or both of the casingsheet supplies to join them to one another, thereby sealing in thetow/SAP composite. Other uses of adhesives will be apparent to thoseskilled in the art based on the teachings provided herein.

[0113] A preferred adhesive for these and other embodiments is H2561Uhot melt construction adhesive, available from Atofindley of Wauwatosa,Wis. Other suitable adhesives, known in the art, may be used providedthey do not excessively impair the desired properties of the casingsheet material (as described elsewhere herein), or add excessivestiffness to the absorbent core 6. For example, other adhesives mayinclude HL-1258 by H. B. Fuller Company of St. Paul, Minn.; Findley 2031and H2587-01 by Ato Findley Inc. of Wauwatosa, Wis.; and NS34-5665 byNational Starch Co. of Bridgewater, N.J. Other adhesives that may beused include 34-578A by National Starch Co. of Bridgewater, N.J. Inanother preferred embodiment, the adhesive may be selected to impartdesired properties to the casing sheet supplies 316, 318. For example,an adhesive may be used to render one of the casing sheet supplies 316,318 fluid impervious, opaque, hydrophobic (or hydrophilic), and so on.the adhesive may also be water soluble or have other beneficialproperties. Adhesive applicators that may be used with the presentinvention include spray applicators, such as those provided by NordsonCorporation of Westlake, Ohio, or other suitable applicators, as areknown in the art.

[0114] Still referring to FIG. 3, in a preferred embodiment theabsorbent core composite 348 is assembled in four procedures that takeplace as the various parts of the assembly are pulled onto the rotatingvacuum draw roll 322. In the first step, which takes place at locationA, the first casing sheet supply 316 is drawn onto the vacuum draw roll322. In the second step, at location B, the opened tow 312 is drawn ontothe vacuum draw roll 322 to overlay the first casing sheet supply 316after being pulled out of the forming jet assembly 304. In the thirdstep, at location C, a supply of SAP 326 is deposited onto the openedtow 312 by the vibratory feeder 332, as described herein. And in thefourth step, at location D, the second casing sheet supply 318 isbrought in to overlie the first casing sheet supply 316, opened tow 312and deposited SAP. Those skilled in the art will appreciate that thesesteps may be performed using equipment other than that specificallydescribed herein, and may also be performed in various different orders,with some of the steps being rearranged, omitted or combined, or withadditional steps being performed. Such variations are generally withinthe scope of the present invention.

[0115] Also in a preferred embodiment, a lay on roll 330 is used topress the second casing sheet supply 318 against the tow/SAP compositeand the first casing sheet supply 316. The lay on roll 330 helps flattenthe core assembly and improves the edge seals between the first andsecond casing sheet supplies 316, 318. The lay on roll 330 may also beequipped to provide ultrasonic, heat, or other bonds between one or moreof the first and second casing sheets 316, 318 and the tow/SAPcomposite. In such an embodiment, the lay on roll 330 may cooperate withthe vacuum draw roll 322 or other device to create the desired bonds.For example, portions of the lay on roll 330 may form ultrasonic horns,while corresponding portions of the vacuum draw roll 332 form ultrasonicanvils that, together, form an ultrasonic bond between the first andsecond casing sheet supplies 316, 318.

[0116] The superabsorbent particles preferably are provided by avibratory feeder 332. The vibratory feeder 332 comprises a feed tray 334that is attached to and driven by a motor 340. The motor 340 vibratesthe feed tray 334, moving it back and forth in the direction ofvibration V, as indicated by the double-headed arrow in FIG. 3. The feedtray 334 is supplied from above by a hopper 336 by way of a flexiblecoupling 338 that helps isolate the hopper 336 from the movement of thefeed tray 334. The vibratory feeder is preferably suspended on one ormore, and most preferably three, scales 342 that weigh the vibratoryfeeder 332 and its contents. The vibratory feeder 332 is preferablypositioned so that none of its moving parts, particularly the motor 340and feed tray 334 strike other parts of the machinery during operation.

[0117] The hopper 336 is preferably selected to provide consistent flowcharacteristics for a variety of superabsorbent polymers or otherparticulate and fibrous additives. In particular, it is preferred thatthe hopper 336 should flow all of its contents in a regular manner,described as “mass flow,” so that few or none of the particles becomestuck in the hopper 336, and do not experience sudden surges in the flowrate. Mass flow is present when essentially all of the material in thehopper is in motion whenever any material is withdrawn. This type offlow pattern is also described as first-in-first-out flow. In order toprovide the desired mass flow, the hopper 336 is preferably designed toavoid “bridging” (i.e., when particles become lodged in the hopper byforming a “bridge” or arch-like structure that resists flowing), and toavoid “ratholing” (i.e., when a column of particles flows through thecenter of the hopper 336, but those particles along the walls do notflow). When the hopper 336 provides mass flow, it is not necessary toprovide undesirable external forces, which may damage or redistributethe particles, to shake unmoving particles free. Mass flow may beobtained by providing the hopper 336 with relatively smooth interiorwalls and by avoiding the use of shallow flow angles within the hopper336. The design may vary depending on the particulate matter or SAP 326being held in the hopper 336, and it may be desirable to test theproperties of the material, such as the material's slip angle and angleof repose, to obtain a suitable hopper design. The design of mass flowhoppers is generally known in the art, and a skilled artisan will beable to design a suitable hopper without undue experimentation based onthe teachings provided herein.

[0118] In one embodiment, the hopper has a capacity of about 1.5 ft³ toabout 10 ft³, and more preferably about 2.25 ft³ to about 6 ft³, andmost preferably about 3 ft³. Also in a preferred embodiment, the hopper336 discharges through an outlet having a diameter of about 4 inches toabout 12 inches, and more preferably about 5 to about 9 inches, and mostpreferably about 7 inches. The hopper 336 may be supplied and refilledwith SAP using any device and method known in the art. In a preferredembodiment, the hopper 336 is filled by a screw (or “auger”) typeconveyor that moves SAP from a supply source into the hopper 336. Thedesign of such hoppers 336, conveyors and supply sources is known in theart, and a skilled artisan will be able to provide a hopper 336 for usewith the present invention without undue experimentation based on theteachings provided herein.

[0119] In a preferred embodiment, the hopper 336 is derived from aSOLIDSFLOW MODEL 5007 DRY MATERIAL FEEDER. Also in a preferredembodiment, the hopper 336 is supplied and refilled from a SOLIDSFLOWMODEL SBS BULK BAG DISCHARGE STATION using a FLEXICON flexible screw(auger) conveyor, which is controlled by a SOLIDSFLOW MODEL 1200LOSS-IN-WEIGHT CONTROLLER. All of these devices are available fromSolidsFlow Corporation of Fort Mill, S.C.

[0120] The vibratory feeder 332 may be suspended from one or more, andmost preferably three, scales 342 that measure the weight of thevibratory feeder 332 and its contents. The scales may be used tocalculate the amount of SAP 326 that is being distributed onto theopened tow 312. Such systems are commonly known as “loss-in-weight”systems, as they continuously measure the reduction in weight of thevibratory feeder 332 as its contents are being emptied. The conveyorsand supply sources that feed into the hopper 336 may also be suspendedon scales so that SAP may be added to the hopper during operation, whilestill being able to calculate the amount of SAP being deposited onto theopened tow 312. In a preferred embodiment, the loss-in-weightmeasurements of the scales 342 are used with a closed-loop feedbackcircuit to control the amount of SAP 326 that is deposited onto theopened tow 312. Such a circuit is preferably integrated into a controlsystem 320 that may control other features and operation of thevibratory feeder 332 and related devices. The scales 342 may also beused to determine when it is necessary or desirable to refill thehopper.

[0121] The scales 342 are preferably able to read to an accuracy thatallows useful determination of the amount of SAP being deposited ontothe opened tow 312. In a preferred embodiment, the scales 342 read to anaccuracy of about +/−10 grams, and more preferably of about +/−1 gram,and most preferably of about +/−0.1 gram. In a preferred embodiment, thescales 342 comprise strain gauge-type load measurement cells, such asthose available under the designation SOLIDSFLOW MODEL 1000 SCALEASSEMBLY from SolidsFlow Corporation of Fort Mill, S.C. The design,construction, and use of scales suitable for use with the presentinvention is known in the art.

[0122] A flexible coupling 338 preferably joins the hopper 336 to thefeed tray 334. The flexible coupling 338 is used pass SAP or otheradditives from the hopper 336 to the feed tray 334, while simultaneouslyisolating the hopper 336 from the vibratory movement of the feed tray334 and motor 340. The flexible coupling 338 may comprise any durableflexible material, such as canvas and other cloths, or natural orsynthetic rubbers. It is preferred that the flexible coupling does notdamp or impede the desired vibrating motion of the feed tray 334 andmotor 340, and thereby impair the ideal SAP feeding. For example, if theflexible coupling 338 is too rigid, it will reduce the ability of themotor 340 to vibrate the feed tray 334 because it will resistdeformation, effectively increasing the mass of the feed tray 334. Also,if the flexible coupling 338 is too elastically resilient, it will tendto store energy created in it when the feed tray 334 and motor 340 arevibrating, and return this stored energy in an uncontrolled manner(i.e., vibrate on its own) thereby creating additional uncontrolledvibrations in the feed tray 334 and motor 340. It also is preferred thatthe flexible coupling 338 be as light as possible so as to reduce theinertia that must be overcome by the motor 340 during operation. In apreferred embodiment, the flexible coupling 338 comprises a rubbermaterial having a diameter and shape selected to join the outlet of thehopper 336 with the inlet chute 402 of the feed tray 334.

[0123] The feed tray 334 and motor 340 preferably are suspended belowthe hopper 336 by flexible mounts 344 that allow the motor 340 and feedtray 334 to move relative to the hopper 336. The flexible mounts 344 maycomprise rods having flexible or pivoting couplings joining them, ateach end, to the hopper 336, motor 340 and feed tray 334. In a preferredembodiment, the flexible mounts 344 are designed to convey a minimalamount of vertical movement or vibration to the hopper 336, which maycause the scales 342 to read inaccurately. In such a preferredembodiment, the flexible mounts 344 may be joined to one or more of thehopper 336, motor 340 and feed tray 334 by a dry or liquid-filledelastomeric bushing or coupling. The design and selection of suchvibration- and movement-damping couplings are known in the art, and askilled artisan will be able to select or produce an appropriatecoupling system based on the teachings provided herein.

[0124] Referring now to FIG. 4, the feed tray 434 preferably comprisesan inlet chute 402 that is attached to the flexible coupling 338 toreceive SAP 326 from the hopper 336. A pan 404 extends away from theinlet chute 402 at a downward angle a to an outlet edge 406 of the feedtray 334. The pan 404 may also comprise multiple sections that descendat varying angles. The feed tray 334 preferably is covered along most ofits length to prevent disturbances of the SAP 326 or other particulateadditives. The covered portion preferably terminates at an adjustablegate 408 located near the outlet edge 406 of the feed tray 334. Theadjustable gate 408 is spaced above the pan 404 and generally dividesthe feed tray into an upstream portion from which the SAP 326 flows anda downstream portion. The adjustable gate 408 may be operated manually,or may be opened and closed by an actuating device, such as anelectromechanical, mechanical, pneumatic, or hydraulic device. Such anactuating device may optionally be controlled by a control system 320using a closed-loop feedback algorithm or open-loop algorithm. Suchactuating devices are known in the art, and a skilled artisan will beable to employ a suitable actuating device without undueexperimentation. Of course, in one embodiment the gate may be a fixedgate, rather than an adjustable gate.

[0125] In a preferred embodiment, the SAP 326 or other particulateadditive material exits the feed tray 334 at its outlet edge 406 in acurtain-like stream having a consistent flow rate across its entirewidth. Referring to FIG. 7, the active width W_(A) of the feed tray 334is the width of the portion of the feed tray 334 from which the SAP 326flows (which may be affected by the use of SAP guides 410, as describedelsewhere herein), and generally corresponds to the width of the SAPflow. The active width W_(A) may vary from one application to the next,and may be varied during operation by using, for example actuatedpivoting SAP guides 410 that move together and apart under the controlof a control system 320. Generally, the active width W_(A) preferably isas approximately the same width as the opened tow 312. In one embodimentactive width W_(A) is about 2 inches to about 12 inches, and is morepreferably about 3 inches to about 10 inches, and, in a particularlypreferred embodiment, the active width W_(A) is as about 3.75 inches toabout 4 inches.

[0126] In other embodiments it may be desirable to vary the flow rate ofthe SAP 326 in particular areas to provide zoned absorbency. Referringnow to FIG. 8, the pan 404 may be contoured or shaped to provideconcentrated flows of SAP during operation or to otherwise control theflow of the SAP. For example, in one embodiment the pan 404 may have oneor more depressions 1502 along the outlet edge 406 that effectivelyincrease the downward angle a at the depressions 1502. In such anembodiment, the SAP 326 may tend to funnel into the depressions 1502,and those portions of the opened tow 312 that pass beneath thedepressions 1502 should receive a relatively high concentration of SAP326. In another embodiment, the pan 404 may have troughs 1504 thatextend below the adjustable gate 408, effectively increasing the heighth of the adjustable gate 408 at those points to increase the flow rateof SAP through the troughs 1504. Such troughs 1504 may extend to theoutlet edge 406 to additionally act as depressions 1502, as describedabove. Other variations in the outlet edge 406 and pan 404 geometry willbe apparent to those skilled in the art based on the teachings providedherein.

[0127] In one embodiment, the feed tray 434 may have more than one inletchute 402 so that a number of different supplies of SAP may be fed intoit. The supplies of SAP may comprise different types of SAP that areblended or isolated from one another using internal baffles and guides.In such an embodiment, for example, one type of SAP may be distributedto the lateral sides of the opened tow 312, and another type of SAP maybe distributed to the central region of the opened tow 312. Othervariations and uses of a feed tray 334 having multiple inlet chutes 402will be apparent to those skilled in the art based on the teachingsprovided herein.

[0128] SAP guides 410, comprising vertical or angled strips of material,optionally may be integrated into the feed tray 334 on either side ofthe adjustable gate 408 to serve a number of purposes. The SAP guidesare preferably attached to the pan 404, but may also be attachedelsewhere to the feed tray 334 or to other objects. In a preferredembodiment, the guides contain the lateral movement of the SAP 326 sothat it falls only in a center region of the opened tow 312. In anotherpreferred embodiment, the SAP guides 410 isolate the flow of SAP 326from turbulent airflow around the feed tray 334 to provide more even SAPdistribution. The SAP guides 410 may be proximal to the outlet edge 406,as shown in FIG. 4, or may be located elsewhere on the pan 404. The SAPguides 410 may also be used to isolate or blend different supplies ofSAP. In one embodiment, the SAP guides 410 may also comprise additionalvertically stacked layers, in addition to the pan 404, that may containseparate flows of SAP. In a preferred embodiment, the SAP guides 410 arespaced apart by about 3.75 inches to about 4 inches to provide about a3.75 inch to about 4 inch wide flow of SAP.

[0129] Referring now to FIGS. 5A and 5B, the feed tray 334 operates onthe principle that particulate solids within them, such as SAP 326, willrest at their angle of repose until disturbed by vibrations induced bythe motor 340. This principle of operation is more fully disclosed inU.S. Pat. No. 3,973,703 to Peschl, which is incorporated by referenceherein in its entirety and in a manner consistent with the presentinvention (hereafter referred to herein as “Peschl”). It should beunderstood that, although the inventors provide various theories on themodes of operation of the vibratory feeder 332, the invention is notintended to be limited to these or other modes or theories of operation.

[0130] It has been found that the flow of the SAP 326 generally may beinfluenced by the properties of the SAP, the downward angle a of the pan404, the rate of vibration of the motor 340, the trailing distance d ofthe pan 404, and the height of the adjustable gate 408. In theembodiment shown in FIG. 5A, the feed tray 334 is shown at rest, withthe SAP 326 being contained within the feed tray 334. In the embodimentof FIG. 5A, the downward angle a is greater than the angle of repose ofthe SAP 326, and so any SAP remaining along the trailing distance d ofthe pan 404 slides off the pan 404 after the motor 340 stops vibrating.The remaining SAP 326 is caught behind a bridge 502 of SAP that forms byfriction between the particles of SAP, cohesion between the SAPparticles, or both. The adjustable gate height h may be adjusted toprovide ideal SAP containment and control. Raising the adjustable gate408 generally provides a greater SAP flow rate for a given motorvibration frequency, while lowering the adjustable gate 408 generallyprovides the opposite result. The adjustable gate height h preferably isadjusted to ensure that a bridge 502 forms promptly after the motor 340stops vibrating the feed tray 334 to stop the flow of SAP 326 as quicklyas possible.

[0131] The flow rate of the SAP generally follows the vibration rate ofthe motor 340, and stops flowing almost immediately upon shut down ofthe motor 340. Generally, faster motor vibration rates provide greaterSAP flow rates and slower motor vibration rates provide a slower SAPflow rate. There is little or no appreciable time delay between changesin the motor frequency and the flow rate of the SAP 326, so thevibratory feeder 332 provides relatively accurate control of the SAPflow, especially when compared to known methods of distributing SAP ontoopened tow 312 or fluff pulp.

[0132] It should be noted that SAP remaining on the trailing distance dof the pan 404 may continue to flow at an uncontrolled rate after themotor frequency changes, but such lag time has not been found to causean appreciable detriment to the device's ability to accurately depositSAP 326 onto the opened tow 312. If a detriment is found, however, thetrailing distance d may be reduced to make the SAP flow rate follow themotor frequency variations more closely. Reducing the trailing distancemay also increase the flow rate of the SAP for a given motor frequencyand adjustable gate height h, as is explained in more detail in Peschl.In one embodiment, the trailing distance may be reduced to zero, and theoutlet edge 406 even may be within the upstream portion of the feed tray334 (i.e., the adjustable gate 408 may be located beyond the outlet edge406).

[0133] In a more preferred embodiment, shown in FIG. 5B, the downwardangle a may be less than the SAP's angle of repose and slip angle (i.e.,the angle at which the SAP 326 will slide down the surface of the pan404), so that when the feed tray 334 is at rest the SAP remaining alongthe trailing distance d stays on the pan 404. In such an embodiment, theaforementioned lag between SAP flow and motor frequency changesassociated with the SAP located in the trailing distance d may bereduced.

[0134] Referring back to FIG. 4, it has been found that the feed tray'soutlet edge 406 should be located as close as possible to the vacuumdraw roll 322. Reducing the offset distance c between the outlet edge406 and the vacuum draw roll 322 provides a number of benefits. Inparticular, minimizing the offset distance c allows the SAP to fall ontothe opened tow 312 as quickly as possible, minimizing any redistributionor diffusion of SAP 326 that may be caused during a longer fall byturbulent air flowing around the feed tray 334 and by interactionbetween the SAP particles 326. Reducing the offset distance c alsodecreases the lag time between changes in motor speed 340 and changes inthe amount of SAP 326 being distributed to the opened tow 312. In apreferred embodiment, the offset distance is about 0.25 inches to about4.00 inches, and more preferably about 0.375 inches to about 1.00 inch,and most preferably about 0.50 inches.

[0135] The minimum value for the offset distance c may be affected bymachine operating tolerances, such as to prevent contact between theopen tow 312 or the vacuum draw roll 322 and the vibrating feed tray334, or by other factors, such as the tolerances of the casing sheetsupplies 316, 318 and opened tow 312. For example, in a preferredembodiment, the offset distance c is at least about 0.50 inches to allowpassage of clumped aggregations of opened tow 312, that may be presentduring startup and during other operating conditions.

[0136] In a preferred embodiment that may be used with a variety ofSAPs, the downward angle α, as measured relative to horizontal, is about10 degrees to about 45 degrees, and more preferably about 12 degrees toabout 30 degrees, and most preferably about 15 degrees. Also in apreferred embodiment, the adjustable gate height h is about 0.10 inchesto about 1.00 inches, and more preferably about 0.125 inches to about0.75 inches, and most preferably about 0.25 inches to about 0.50 inches.Also in a preferred embodiment, the trailing distance d is about 0.25inches to about 8 inches, and more preferably about 2 to about 6 inches,and most preferably about 4 inches. Also in a preferred embodiment, theinlet chute 402 has a diameter of about 4 inches to about 12 inches, andmore preferably about 5 to about 9 inches, and most preferably about 7inches. In a preferred embodiment, the feed tray 334 may be derived froma SOLIDSFLOW MODEL 5000 DRY MATERIAL FEEDER, available from SolidsFlowCorporation of Fort Mill, S.C.

[0137] Referring now to FIGS. 6 and 7, the feed tray 334 preferably isequipped with side plates 602 that help isolate the SAP 326 and openedtow 312 from lateral airflow and may help contain the lateral movementof SAP 326 after it exits the feed tray 334. Such lateral airflow andother airflow may disturb the desired distribution of SAP onto theopened tow 312. The side plates 602 are preferably orientedapproximately parallel to the machine direction of the opened tow 312(i.e., within about 20 degrees of parallel) and sized to substantiallyreduce or block air from flowing laterally into the area beneath thefeed tray 334. Preferably, a first edge 604 of each side plate 602 islocated proximal to the vacuum draw roll 322 (or other similar drawingdevice); and a second edge 606 of each side plate 602 is locatedproximal to the forming jet assembly 304. The side plates 602 arepreferably shaped and sized so that they do not strike any other partsof the machine as they are vibrated back and forth. A third edge 608 ofeach side plate 602 preferably is adapted to conform to the secondcasing sheet supply 318 to help prevent lateral airflow from above thefeed tray from encroaching upon the supply of SAP 326. In such anembodiment, it also may be desirable for the top edge 610 of theadjustable gate 408 to be proximal to the second casing sheet supply 318to further reduce the amount of air that flows in to potentially disturbthe SAP 326. The SAP guides 410 may also have an edge 612 contoured tobe adjacent to the second casing sheet supply 318 to further inhibit thedevelopment of undesirable airflow near the SAP 326. The side plates 602preferably may be adjusted in at least the vertical direction, asindicated by the double-headed arrow in FIG. 6. In other embodiments,the side plate 602 may be attached to something other than the feed tray334, but in such embodiments, care should be taken to prevent the movingfeed tray 334 from striking the side plates 602 during operation.

[0138] Referring back to FIG. 4, the motor 340 is used to initiate andmodulate the flow of SAP 326 out of the feed tray 334. The motor 340vibrates the feed tray 334 by moving it back and forth in the directionof vibration V, as indicated by the double-headed arrow in FIG. 4. In apreferred embodiment, both the pitch p and frequency of the motor 340may be adjusted to modulate the flow of SAP 326. It has been found thatincreasing the motor's pitch p (i.e., the distance traversed by themotor during each cycle) generally increases the SAP flow rate, andvice-versa. Also, as noted before, it has been found that increasing themotor's frequency generally also increases the SAP flow rate, andvice-versa.

[0139] The effectiveness of the motor 340 and amount of control providedby the motor 340 are affected by the weight and rigidity of the feedtray 334. If the feed tray 334 is too heavy, its inertia will resist theforces imparted upon it by the motor 340, and the motor 340 may not beable to accelerate and decelerate it back and forth to create thedesired pitch p distance or frequency vibrations. If the feed tray 334is not rigid enough, it will flex as the motor 340 imparts forces on it.As the feed tray 334 flexes, it absorbs the energy that was intended tomove the feed tray 334 and does not accurately follow the path intendedby the motor 340. The energy absorbed by a flexible feed tray 334 may bereleased in the form of undesirable variations in the intended pitch pand frequency of vibration. It has been found that it is generallydesirable to make the feed tray 334 as light and as rigid as possible inorder to provide the greatest amount of control of the SAP flow.

[0140] In a preferred embodiment, the motor 340 is coupled to the feedtray 334 through a coupling 412. In order to provide accuratetransmission of the motor's vibrations to the feed tray 334, thecoupling 412 should be rigid in the vibration direction V, and thecoupling 412 preferably has a box-like shape or C-shape. Also in apreferred embodiment, the inlet chute 402, which may comprise arelatively large open space that may be susceptible to undesirableflexing, is reinforced with a structural member, such as a tubular brace414 aligned in the vibration direction V. In an embodiment in which theinlet chute has a diameter of about 7 inches it has been found that atubular brace 414 of about 1 inch diameter is suitable to reduceundesirable flexure in the inlet chute 402 without adversely affectingthe flow of SAP through the inlet chute. In other embodiments, in whichthe inlet chute 402 contains baffles or other internal flow-directing orflow-controlling structures (as shown in FIG. 17), these structures mayalso serve to increase the feed tray's rigidity, making it unnecessaryto reinforce the inlet chute 402.

[0141] As noted before, the motor 340 and feed tray 334 are suspendedbeneath the hopper 336 by flexible mounts 344 that allow both the motor340 and the feed tray 334 to move independently of the hopper 336. Assuch, as the motor 340 vibrates the feed tray 334 back and forth, themotor 340 itself may also move back and forth. In a preferredembodiment, the mass of the motor 340 is significantly greater than thecombined mass of the feed tray 334 and the SAP 326 contained therein,and so the movement of the motor 340 will be insignificant relative tothe movement of the feed tray 334. In such an embodiment, the motor'spitch p will be almost entirely converted into movement of the feed tray334 (as is shown in FIG. 4). If, however, the motor 340 does experiencea significant amount of movement, more of the pitch p will be convertedinto the motor's movement, and less of the pitch will result in movementof the feed tray 334. This reduction in the movement of the feed tray334 may result in less effective SAP distribution and control. If it isfound that the movement of the motor negatively affects the SAPdistribution and control, the motor's movement may be restricted, or thepitch p may be increased to increase the effective movement of the feedtray 334. Other measures may also be taken to counteract such negativeaffects. Those skilled in the art will be able to measure or calculatethe movement of the motor 340 and feed tray 334 and make accommodationsin the design of the apparatus for such movements using the teachingsprovided herein.

[0142] In a preferred embodiment, the motor 340 comprises anelectromagnetic vibrator, such as those supplied by Eriez, Corporationof Erie, Pa. as Model Number 30A, part number 3N-56743. Such a motor maybe selected to be driven by any available power source, such as a 115volt, 60 Hz power source. The motor may also require specific support ordrive hardware and software, such as an Eriez VTF signal followingcontroller board that is supported by and AB SLC 0-20 mA analog card,available from Allen-Bradley Company of Milwaukee, Wis. Other motors 340may also be used, such a rotary motor that is configured to providecyclical lateral movement or vibrations to the feed tray 334. Otheruseful motors 340 include pneumatic, magnetic, electric and hydraulicactuators, and the like, as long as they can provide the necessaryforces to vibrate the feed tray 334 at the desired pitch p andfrequency. Electromagnetic vibrators are preferred, as they typicallyprovide relatively controllable movement and consume less energy thanother devices.

[0143] In one embodiment that should be suitable for dispensing avariety of SAP materials, the motor 340 may be operated from astandstill (zero Hz) up to about 430 Hz, and more preferably up to about520 Hz, and most preferably up to about 600 Hz. In a preferredembodiment that should be suitable for dispensing a variety of SAPmaterials, the frequency is approximately constant, and the flow rate ofthe particulate matter is controlled by modulating the motor's pitch. Insuch a preferred embodiment, the motor frequency is about 60 Hz, and thepitch p of the motor variable between about 0.01 inches to about 0.125inches, and more preferably about 0.02 inches to about 0.10 inches, andmost preferably about 0.04 inches to about 0.08 inches. Such adjustmentsmay be obtained, for example, by varying the voltage of the motorbetween about 0 and about 90 volts.

[0144] Such a vibratory feeder 332 may be adapted to provide a highvolume of SAP flow, and may be used at relatively high manufacturingline speeds. It is anticipated that a vibratory feeder producedaccording to a preferred embodiment of the present invention may be usedwith an assembly line producing diapers at a rate in excess of 600products per minute. The vibratory feeder 332 preferably can feedsuperabsorbent polymer or other additives at a rate of about 10,000grams per minute (g/min) to about 20,000 g/min, and more preferably at arate of about 12,500 g/min to about 17,500 g/min, and most preferably ata rate of about 15,000 g/min. In a preferred embodiment, the hopper 336is fed by a screw-type conveyor or other conveyor that has a capacity tomaintain a useful level of SAP 326 in the vibratory feeder 332. Theconveyor may have a feed rate that is less than the maximum feed rate ofthe vibratory feeder 332, so long as the average feed rate of thevibratory feeder 332 does not exceed the average feed rate of theconveyor.

[0145] Superabsorbent polymers and other particulate additives can berelatively expensive, and so it is often desirable to minimize theamount of SAP that is placed in the core and to “zone” such additivesonly where they are most beneficial for the final product. Such zoningis also particularly beneficial in tow-based absorbent cores because thelack of fluff pulp in such cores may reduce the overall wickingcapability of the core, making it more important to place the SAP closerto the location where fluid is likely to strike the garment. In apreferred embodiment, the motor 340 is controlled by a control system320 to provide a desirable distribution of SAP 326 into the opened tow312. In one preferred embodiment, such a control system 320 may be usedto operate the motor 320 to deposit a steady stream of SAP 326 onto theopened tow 312 to provide a uniform opened tow/SAP mixture in theabsorbent cores that are ultimately formed by the process. In anotherpreferred embodiment, the control system may cyclically increase anddecrease the pitch p and/or frequency of the motor 340 to deposit apulsating supply of SAP 326 to the opened tow 312, thereby providing theabsorbent cores with targeted concentrations of SAP that provide thegarment 10 with zoned absorbency. Preferably, the control system 320uses a closed-loop feedback method that considers various factors indetermining how much SAP to distribute at any given moment.

[0146] In a preferred embodiment, the control system 320 is providedwith information about how fast the assembly line is running by using,for example, a tachometer 346 on the vacuum draw roll 322 or by anyother suitable line speed measuring device (See FIG. 3). By integratingsuch a line speed measuring device into the control system 320, thecontrol system 320 may be programmed to increase or decrease the pitch por frequency of the motor 340 to vary the SAP flow rate as the productmanufacturing rate changes, thereby providing all of the products withthe proper amount of SAP, regardless of the assembly line speed. Such acapability provides a lower rate of product rejection duringtransitional phases, thereby improving the overall efficiency of themanufacturing process.

[0147] In another preferred embodiment, the output of the scales 342 isintegrated into the control system 320. By considering the weight of theSAP being distributed, as measured by the scales 342, the control system320 may programmed to modulate the motor 340 to accurately distributeSAP at the desired flow rate. In such an embodiment, the control system320 may also accommodate for deviations in the flow characteristics ofthe SAP particles to continue to provide an even flow, such as byincreasing the vibration rate if it is found that the SAP is not flowingas rapidly as expected, and vice-versa. Such deviations may be caused bytypical variations in the shape, size, humidity, density, or otherfeatures of the SAP, or may be caused when a different SAP product isused in a machine that was originally set up for another type of SAP orset up for a SAP provided by a different supplier.

[0148] A closed-loop feedback control system 320 may also be programmedto stop distributing SAP in the event that a fault is detected in theprocessing line. For example, if a fault detection circuit tied into thecontrol system 320 determines that one or more products will bedefective upon completion, the flow of SAP may be stopped so that thedefective products will not receive SAP. In such an embodiment, it maybe desirable to produce the absorbent cores of the garments as late aspossible in the manufacturing process in order to detect as many defectsas possible before preparing the absorbent core 6 for each product.

[0149] In one embodiment, a SAP concentration detection device 350 (FIG.3) may be integrated into the control system 320 to provide furtherdetection and control capabilities to the control system 320. Theconcentration detection device 350 may be located to measure the amountand/or location of SAP in the assembled absorbent core composite 348. Ifthe amount of location of the SAP is not present as desired, theconcentration detection device 350 may signal this to the control system320 so that appropriate corrections in the SAP feed rate may be made.Those skilled in the art are capable of designing or utilizing asuitable SAP concentration detection device 350 using the guidelinesprovided herein.

[0150] The flow rate of the SAP may also be controlled by a controldevice 320 by actively adjusting the height h of the adjustable gate 408during operation. As noted before, the adjustable gate 408 may be raisedand lowered during operation to increase and decrease, respectively, theflow rate of the SAP 326. Such adjustments may also be made to provide acyclically fluctuating amount of SAP to the opened tow 312 to createtargeted regions of relatively high SAP concentration for zonedabsorbency. In such an embodiment, the control device 320 may operatethe adjustable gate 408 in conjunction with the scales 342, tachometer346, concentration detection device 350, or other sensors to provideclosed-loop feedback control of the SAP flow. A suitable actuationdevice for cyclically raising and lowering the adjustable gate 408preferably does not cause excessive vibrations or other movements thatmay cause the scales 342 to read inaccurately.

[0151] Referring now to FIG. 9, it has been found that a “combiningdrum”-type vacuum draw roll 800 may be advantageously used inconjunction with vibratory feeders 332, such as those described herein,or, alternatively, with other SAP feed devices and methods, such asthose that are known in the art. The combining drum 800 is characterizedin that several or all of the parts that eventually form the absorbentcore 6 of the garment 10 are assembled in a continuous motion around allor part of the combining drum's circumference. In a preferredembodiment, the combining drum 800 combines the first casing sheetsupply 316, opened tow 312, SAP 326 and second casing sheet supply 318(i.e., various constituent parts of the core composite 348, which may,of course, include other parts) in a substantially continuous operationas they are conveyed by the combining drum 800. Each of the parts may beconveyed to the combining drum 800 separately and then joined togetherinto an integrated structure, or alternatively, some of the parts may bejoined to one another prior to contact with the combining drum 800. Forexample, an additional layer 20 may be affixed to either side of one orboth of the first and second casing sheet supplies 316, 318 before thesupply is provided to the combining drum 800.

[0152] As noted before, a preferred combining process has been generallydescribed elsewhere herein with reference to Locations A, B, C and D ofFIG. 3. The operation of the combining drum 800 described herein isrelatively simple compared to many known core-forming apparatus, and maybe adapted to operate at high line speeds. For example, it isanticipated that the combining drum 800 may be adapted to operate withan assembly line producing in excess of 600 diapers per minute.

[0153] In a preferred embodiment the combining drum 800 has a generallycylindrical surface 802 with a vacuum surface 804 forming acircumferential belt on the cylindrical surface 802. The vacuum surface804 comprises one or more holes 806 through which a vacuum is applied tothe various parts of the core composite 348. The holes 806 in the vacuumsurface 804 may be formed by any means known in the art, such asdrilling, machining, casting and so on. In a preferred embodiment, theholes 806 have a diameter of about 0.0625 inches to about 0.75 inches,and more preferably of about 0.125 inches to about 0.625 inches, andmost preferably of about 0.25 inches to about 0.50 inches. Also in apreferred embodiment, the holes may be spaced from one another by acenter-to-center distance of about 0.10 inches to about 1.00 inch. Theholes may be spaced in a rectilinear array, as staggered rows, or in anyother pattern that conveys the desired amount of vacuum. The vacuumsurface 804 also may comprise any other relatively rigid foraminousstructure, such as one or more mesh screens or removable perforatedplates that are affixed to openings in the cylindrical surface 802. In apreferred embodiment, the combining drum 800 may also comprise landingareas 808 on either side of the vacuum surface 804 which may be treatedto enhance their ability to grip the first and second casing layersupplies 316, 318. A vacuum is applied to the combining drum 800 througha vacuum port 810.

[0154] Referring now to FIG. 10, there is shown a sectional view of thevacuum surface 804 region of a combining drum 800 as is appears justafter combining the first casing sheet supply 316, opened tow 312, SAP326 and second casing sheet supply 318 into an integrated core composite348. The width W₁ of the vacuum surface 804 (as measured in a directionparallel to the rotational axis of the combining drum 800) preferablycorresponds approximately to the width of the opened tow 312 and to thewidth of the portion of the feed tray 334 from which SAP 326 isprovided. The first and second casing sheet supplies 316, 318 arepreferably wider than the opened tow 312, and their excess width islocated in side areas 902 that overlie the landing areas 808. The firstand second casing sheet supplies 316, 318 preferably are joined to oneanother in their side areas 902 by adhesive bonding, other methodsdescribed elsewhere herein or by other methods known in the art. Asnoted elsewhere, a lay on roll 330 may be used to help join the firstand second casing sheet supplies 316, 318 by use of pressure, crimpingnodules, and the like.

[0155] In a preferred embodiment, the vacuum surface 804 is recessed inthe cylindrical surface by a depth y of less than about 0.50 inches, andmore preferably by less than about 0.10 inches, and most preferably byabout 0.030 inches. It has been found that having a slight increase inthe diameter of the combining drum 800 on either side of the vacuumsurface 804 (i.e., a recessed vacuum surface 804) helps keep the firstcasing sheet supply 316 stretched across the combining drum 800 duringoperation.

[0156] The vacuum surface width W₁ may be selected to provide certainbenefits to the garment into which the core composite 348 is beingintegrated. In one embodiment, the core composite may be integrated intothe garment in a flat state, in which case it may be desirable to makethe vacuum surface width W₁ and the width of the opened tow 312 equal tothe desired width of the garment's absorbent core 6. However, the corecomposite 348 may be stretched, folded, or otherwise resized duringmanufacture, in which case the vacuum surface width W₁ should becorrespondingly adjusted. In a preferred embodiment, the core composite348 is folded at least once before being integrated into the garment.Folded absorbent cores have been discussed in more detail elsewhereherein. In a preferred embodiment, the vacuum surface width W₁ is about1.75 inches to about 12 inches, and more preferably about 2.75 inches toabout 10 inches, and most preferably about 3.75 inches. In order toreduce SAP loss during core formation, the vacuum surface width ispreferably slightly narrower (about 0.10 inches on either side) than thewidth of the supply of opened tow 312 to promote a slight inwardmigration of SAP away from the side areas 902.

[0157] As noted before, it has been a continuing challenge to providethe desired distribution of SAP within the absorbent cores 6 ofabsorbent garments 10. It has been found that a combining drum 800 asdescribed herein may be beneficially used to help provide such desiredSAP distributions. Cellulose acetate opened tow 312 and other types oflow density fibrous opened tow structures allow a relatively largeamount of air to pass through them compared to conventional fluff pulpmaterials, and the location of the SAP 326 may be effectively controlledby modulating the amount and position of the vacuum applied to theSAP/opened tow mixture. It has been found that the distribution of theSAP can be more easily controlled with tow/SAP cores than with fluff/SAPcores. As air passes through the opened tow 312 into the vacuum itconveys the SAP 326 through the fibrous structure, and the SAP particles326 generally tend to concentrate more densely at areas having a highvacuum. Also, as the vacuum is increased, the SAP particles 326generally move closer to the surface of the opened tow 312 that isadjacent the combining drum 800. The degree to which the SAP migratestowards the high vacuum areas may also be affected by the duration oftime that the vacuum is applied to the SAP 326. The vacuum also helpsprevent SAP 326 from escaping out of the opened tow 312 duringmanufacturing. It has been found that a desirable mixture of SAP 326within the opened tow 312 and reduced SAP loss may be produced using avacuum of about 2.50 inches of water to about 20 inches of water, andmore preferably of about 3.75 inches of water to about 12.5 inches ofwater, and most preferably of about 5.0 inches of water. The vacuum maybe pre-set or may be manually or actively controlled by a control system320 using an open-or closed-loop feedback system.

[0158] In addition to being useful for providing a homogeneousdispersion of SAP 326 in the opened tow 312, a combing drum 800 asdescribed herein may also be used to accomplish various other desirableSAP distribution patterns. In one embodiment, the vacuum level may bemodulated to provide a desirable depth of SAP penetration throughout theopened tow 312 or only in discrete areas of the opened tow 312. In otherembodiments, the combining drum 800 may be adapted to provide machinedirection (MD) and cross-machine direction (CD) zoning of the SAPparticles 326 that provide the garment 10 with zoned absorbency. Themachine direction is the direction in which a part or assembly movesduring processing, and the cross-machine direction is perpendicular tothe MD. The machine direction generally corresponds to the longitudinaldimension 100 of the fully-assembled garment 10 (see FIG. 1), and thecross machine direction corresponds to the lateral dimension 102 of thegarment, however other relationships may also be used and are within thescope of the present invention.

[0159] Referring now to FIG. 11, regions of high SAP concentration, andthus greater absorbency, may be provided in the MD and CD by making thevacuum surface 804 with particularly designed target regions 1002 thatconvey a greater amount of vacuum to portions of the opened tow 312.Such target regions 1002 may have larger holes and/or a greaterconcentration of holes in those areas where a greater concentration ofSAP 326 is desired. The larger amount of open space provided in suchregions will allow a greater amount of airflow into the vacuum, and thuscause a greater amount of SAP to migrate to those areas. For example, inthe embodiment of FIG. 11, the region 1004 has a greater concentrationof larger holes, which should provide a SAP concentration in the portionof the core composite 384 adjacent region 1004. The particular patternof SAP concentration may be adjusted by making each of the targetregions 1002 from a removable plate 1006 having the desired holepattern. Substitute plates 1006 may be easily machined to providedifferent hole patterns and zoned absorbency patterns.

[0160] In another embodiment, shown in FIG. 12, the vacuum surface 804may be separated into discrete target regions 1102, which may havevarying widths, to provide zones of high and low MD and CD SAPconcentrations.

[0161] In an embodiment in which the combining drum 800 has targetregions 1002, 1102 for providing zoned absorbency, the combining drumdiameter D₁ should be selected so that the corresponding parts of eachtarget regions 1002, 1102 are spaced from one another around thecircumference of the combining drum 800 by a distance corresponding tothe absorbent core length X₁. By using such a spacing, each targetregion 1002, 1102 will create a targeted zone of SAP that will beproperly located in each absorbent core 6 that is cut from the corecomposite 348.

[0162] It should be understood that by providing a distance betweencorresponding parts of each target region 1002, 1102 that isapproximately equal to a core length X₁, the circumference of thecombining drum 800 will be sized to equal a whole number multiple of thecore length X₁. At a minimum, the circumference can equal one corelength X₁, but in such an embodiment, the various parts of the corecomposite 348 will be in contact with the vacuum for relatively littletime, which may lead to inadequate SAP distribution or other formingproblems. Smaller diameter drums may also be subject to greatervibration. These problems may become exacerbated when the vacuum drum800 is used with higher speed assembly lines. Problems may also be existwith larger drum diameters. For example, the manufacturing tolerancesfor a larger diameter drum may be less precise. In addition, as the sizeof the drum increases the amount of startup waste may increase,particularly if a greater amount of vacuum is required for the largerdrum, leading to longer vacuum stabilization times. Larger drums thatrequire greater amount of vacuum also may require more power to producethe necessary vacuum. It will be understood that these considerationsalso apply to embodiments of the invention in which the combining drum800 does not have target regions 1002, 1102, such as in the embodimentdepicted in FIG. 9.

[0163] It is preferred, therefore, that the drum diameter D₁ be selectedso that the drum's circumference is large enough that the parts of thecore composite 348 are in contact with the vacuum long enough toproperly distribute the SAP without excessive vibrations, but smallenough to provide the required precision and a minimal amount of startupwaste. It has been found that in a preferred embodiment, the diameter D₁is selected so that the circumference is equal to between three andseven core lengths X₁.

[0164] In a preferred embodiment, the combining drum 800 (whether it hastarget regions 1002, 1102 or not) has a diameter D₁ of about 6 inches toabout 28 inches, and more preferably of about 9 inches to about 20inches, and most preferably of about 12 inches. In this embodiment, thenumber of wasted cores caused by vacuum hysteresis or otherstartup-related issues has been found to be about 5 products perstartup, as compared to up to about 50 products per startup withconventional core forming processes. It has also been found thatproviding the necessary vacuum to such a combining drum 800 requiresabout 10 horsepower to 20 horsepower, whereas conventional core formingsystems require up to about 400 horsepower, and so a significant powersavings is provided.

[0165] Referring now to FIGS. 13 through 15, a preferred embodiment ofthe combining drum is shown in which the combining drum 800 may beconfigured to apply a vacuum to the parts of the core composite 348 onlythrough a portion of the drum's rotation. The combining drum 800 of apreferred embodiment comprises an outer drum 1202 that is positioned torotate about a fixed inner drum 1204 by, for example, being affixed toan axle 1208 that passes through rotary bearings 1210 in the inner drum1204. Such bearings 1210 may be equipped to reduce or prevent theleakage of the vacuum through them. A vacuum is applied to the space1206 inside the inner drum by a vacuum port 810. The vacuum is conveyedto the outer drum's vacuum surface 804 by way of one or more passages1212 through the inner drum 1204 that are preferably located subadjacentthe path of the vacuum surface 804 of the outer drum 1202 to maximizethe strength of the vacuum applied through the vacuum surface 804. Itwill be understood by those skilled in the art that the inner drum 1204may be replaced by any vacuum chamber having one or more passages 1212that convey a vacuum to a location subadjacent all or part of the vacuumsurface 804.

[0166] Only those portions of the vacuum surface 804 that areimmediately adjacent the passages 1212 receive a vacuum, so the durationand location of the vacuum's application may be modified by changing thesize, number, or location of the passages 1212. Referring specificallyto FIG. 14, the passages 1212 may be positioned through an arc of theinner drum 1204 that defines a vacuum zone Θ_(V). The leading edge ofthe vacuum zone 1302 is preferably located proximal to the point atwhich the first casing sheet supply 316 contacts the combining drum,which is designated as Location A in FIG. 3. The trailing edge of thevacuum zone 1304 is preferably located beyond (as the drum rotates) thepoint at which the second casing sheet supply 318 contacts the combiningdrum 800, which is designated as Location D in FIG. 3. Referring now toFIG. 15, it can be seen that those portions of the vacuum surface 804that are not adjacent the passages 1212 are effectively cut off from thepull of the vacuum. After the core composite 348 passes the trailingedge of the vacuum zone 1304 and reaches this blocked-off area it isreleased from the vacuum's hold and conveyed to other parts of theassembly line.

[0167] The size of the vacuum zone Θ_(V) may vary depending on where thevarious parts are desired to be assembled to form the core composite348. In a preferred embodiment, the vacuum zone Θ_(V) is about 45degrees to about 180 degrees, and more preferably is about 90 degrees toabout 160 degrees, and most preferably is about 140 degrees.

[0168] Various devices may be employed with the combining drum 800 tomodulate the location and amount of vacuum applied to the core composite348. In one embodiment, shown in FIG. 14, internal sleeves 1306 or othervalving mechanisms may be used to adjust the points at which the vacuumzone Θ_(V) begins and ends. In another embodiment, shown in FIG. 13,other internal sleeves 1214 or other valving mechanisms may be used tonarrow or widen the width of the vacuum zone Θ_(V), thereby effectivelynarrowing and widening the width W₁ of the vacuum surface 804. In stillanother embodiment, an internal sleeve or other valving mechanism may beused to reduce the vacuum level within all or part of the inner drum1204. Any of such sleeves and valving mechanisms may be actuated by acontrol system 320 under the guidance of an open- or closed-loopfeedback system. Greater or lesser amounts of vacuum may also be appliedin discrete portions of the vacuum zone Θ_(V). Other designs will beobvious to one skilled in the art based on the teachings providedherein.

[0169] A combining drum 800, as described herein, may be used with anySAP feeding device that deposits SAP onto opened tow or other fibrousmaterials. The embodiments of the combining drum 800 described hereinhave been found to be particularly useful when used in conjunction withthe vibratory feeder 332 as described herein.

[0170] The vibratory feeder 332 and combining drum 800 offer severaladvantages over prior art SAP depositing systems. In particular, thevibratory feeder 332 provides improved control over the volume andplacement of the SAP 326 in the opened tow, allowing greater controlover the SAP distribution (and zoned absorbency) during transitionalphases, such as during machine startup, stopping and other speedchanges, leading to fewer rejected products during such times. Inaddition, the vibratory feeder 332 and combining drum 800 provideimproved SAP penetration into the opened tow 312 or other core materialand an improved ability to selective position the SAP to providedesirable zoned absorbency. The vibrator feeder 332 and combining drum800 also provide easier operation, as the various features of eachdevice may be integrated into a control system 320. Stull further, thevibratory feeder 332 and combining drum 800 are relatively simple andreliable devices that require little maintenance or cleaning, therebyreducing the operating cost of the machine. Another advantage of thevibratory feeder and combining drum 800 is that they may be operated athigh line speeds without detriment to the product quality. Otherbenefits will be apparent to those skilled in the art based on theteachings provided herein.

[0171] Referring now to FIGS. 16 and 17, in a preferred embodiment ofthe invention the pan 404 of the feed tray 334 may be modified to“shuffle” back and forth to provide zoned concentrations of SAP 326 orother particulate matter in the supply of opened tow 312 or otherfibrous material. In the embodiment shown in FIG. 16, only a portion ofthe pan 404 is adapted to be a shuttle pan 404′. In the embodiment ofFIG. 17 the entire pan 404 is replaced by a shuttle pan 404′. In eithercase, the shuttle pan 404′ moves along a path substantially parallel (asviewed from above) to the moving supply of fibrous material through astroke distance D_(S) as the feed tray is vibrated, thereby varying theposition of the outlet edge 406 as a function of time. Such a shuttlepan 404′ may be particularly useful to obtain zoned absorbency in casesin which the motor 340 is unable to provide rapid speed changes, or theflow rate of the SAP 326 does not follow the motor's speed changesrapidly enough to accurately create precisely located zones of high SAPconcentration in the core composite 348, as may be the case whenrelatively high manufacturing rates are desired. In some cases, theshuttle pan 404′ may be provided with a directionally-biased surface1704 that encourages or forces movement of the SAP 326 towards theoutlet edge 406.

[0172] The shuttle pan 404′ may be moved by any suitable drive unit andlinkage (not shown) known in the art, provided the movement does notcause vibrations in the vibratory feeder 332 that impair theloss-in-weight measurements of the scales 342 or otherwise reduce theability of the vibratory feeder 332 to accurately dispense SAP 326. Thedrive unit and linkage may require counterbalancing to reduce suchharmful vibrations. The drive unit and linkage preferably are alsorelatively light and compact so that they may be installed on the feedtray 334 without interfering with other parts of the machinery andwithout adding too much weight for the motor 340 to properly vibrate thefeed tray 334. Suitable drive motors may include pneumatic and hydraulicdrives that operate either drive pistons or rotating drives, andelectric motors. The shuttle pan 404′ also should be suspended such thatit can move smoothly back and forth. For example, sliding or rollingguides may be used to mount the shuttle pan 404′ to the feed tray 334.Such guides preferably do not require fluid lubricants (except within asealed area, such as a sealed bearing), as such lubricants may damagethe garments being manufactured or cause irritation in the garments'users. The selection of drive units, linkages, counterbalances andsliding or rolling guides are known in the art, and the presentinvention is not limited to the use of any particular design for each ofthese parts.

[0173] The shuttle pan 404′ may be used with any type of vibratory feedtray 334, including those equipped with an adjustable gate 408, as shownin FIG. 16, or those using baffles 1702 or other internal flow-directingor flow-controlling structures in the inlet chute 402, rather than anadjustable gate 408, as shown in FIG. 17. The use of an adjustable gate408 may reduce the available room for the shuttle pan 404′, therebylimiting the shuttle pan 404′s total stroke distance D_(S). As such, incases in which a larger stroke distance D_(S) is desired, it may bepreferred to replace the entire pan 404 with a full-length shuffle pan404′ and use baffles 1702 to control the flow of SAP 326.

[0174] The goal of the shuttle pan 404′ is to periodically “follow” themotion of the supply of fibrous material so that SAP 326 beingdistributed from the feed tray 334 falls in a greater concentration oncertain portions of the fibrous material. Ideally, these highconcentrations of SAP 326 are ultimately positioned in those portions ofthe garment 10 that are expected to receive the greatest influx of fluid(zoned absorbency). In order to position the high SAP concentrations inthe proper place in the garment 10, the repeating motion of the shuttlepan 404′ should be related to the length X₁ of the absorbent cores 6that are severed from the core composite 348 that is being manufactured.Such correlation is generally obtained by cycling the shuttle pan 404′through its entire range of movement once for each core length X₁ thatpasses through the device. In some cases when the preferred fibrousmaterial (opened tow) is used, however, the length of opened tow 312that ultimately forms each core 6 may, at the time it is imbued with SAP326, be greater or lesser than the final core length X₁. Such may be thecase, for example, if the opened tow 312 is stretched, compacted, orfolded along its length during some manufacturing operation occurringafter the SAP 326 is placed into the opened tow 312, but before theopened tow/SAP combination is placed into the garment 10. In such cases,the cycles of the shuttle pan 404′ may have to be modified to ensurethat the concentrations of SAP 326 are ultimately placed in the correctposition in the garments 10. Those skilled in the art will be capable ofmaking such measurements and modifications without undue experimentationbased on the teachings provided herein.

[0175] The operation of the shuttle pan 404′ is described and depictedwith reference to FIGS. 18A-18E. Each of FIGS. 18A-18E depicts theoperation of the shuttle pan 404′ at successive equal time intervals,with FIG. 18A corresponding to a time of 0×, FIG. 18B corresponding totime 1×, FIG. 18C corresponding to time 2×, and so on. The total cycletime for the shuttle pan 404′ is 4×, and during the cycle, the supply ofopened tow 312 is moving at a substantially constant speed in adirection indicated by the arrow marked “web path”. The flow rate of SAP326 into the feed tray 334 remains substantially constant during alltimes. The particular longitudinal area of the opened tow 312 receivingthe higher concentration of SAP 326 is designated by the arrow markedA_(C) (“concentration area”).

[0176] As can be seen from FIGS. 18A-18C, during the forward stroke ofthe shuttle pan 404′, the pan's outlet edge 406 “follows” theconcentration area A_(C) for a prolonged period. During this period, arelatively large amount of SAP 326 is deposited into the opened tow 312.During the back stroke of the shuttle pan 404′, as seen in FIGS. 18D and18E, the pan's outlet edge 406 moves across a large span of the openedtow 312, depositing a lesser concentration of SAP in those regionsbetween each concentration area A_(C). The cycle then repeats for thenext core length X₁.

[0177] The relative amount of SAP concentration between the highconcentration zones and the low concentrations zones may be adjusted byaltering the stroke distance D_(S). A greater stroke distance D_(S)generally will provide more focused concentrations of SAP 326, and inone embodiment, the stroke distance D_(S) may be as long as half of theabsorbent core length X₁ to provide a relatively large concentration ofSAP 326. In a preferred embodiment, in which the absorbent core lengthX₁ is between about 12 inches and about 18 inches, the stroke distanceD_(S) is about 2 inches to about 13 inches, and more preferably is about4 inches to about 11 inches, and most preferably is about 6 inches toabout 9 inches.

[0178] The shuttle pan 404′ generally should be angled downward to allowthe SAP to flow down it. The selection of such an angle has beendescribed elsewhere herein. The supply of opened tow 312 or otherfibrous material may be substantially horizontal, as shown in FIGS.18A-18E, or may be angled upward or downward, or contoured around thecircumference of a vacuum draw roll 332 or combining drum 800. Theopened tow 312 also may be oriented to be parallel with the shuttle pan404′, and preferably, it is contoured around a combining drum 800, asdescribed elsewhere herein.

[0179] The outlet edge 406 preferably is located by an offset distancec, as described elsewhere herein (FIG. 4), from the device conveying thefibrous material. In those embodiments in which the fibrous material isprovided at an angle relative to the shuttle pan 404′ or around thecircumference of a combining drum 800, the offset distance c between theoutlet edge 406 and the device conveying the fibrous material will varyas the outlet edge 406 moves through its range of motion. In such cases,it is preferred that the maximum offset distance c does not exceed morethan about 300% of the minimum distance c during the stroke of theshuttle pan 404′. Such variations in the offset distance c, orexcessively high offset values may reduce the apparatus' capacity toprovide the desired SAP concentration, because as the SAP falls throughgreater offset distances c wind and the interaction of the SAP particleswith one another may cause uncontrolled dispersion the SAP. The movementprofile of the shuttle pan 404′, as described elsewhere, may be alteredto minimize or reduce the negative consequences of having a varyingoffset distance c. In addition, a varying offset distance c may bebeneficially introduced to the apparatus to provide variations in theSAP concentration.

[0180] The size of the concentration area A_(C) and the relative amountof SAP concentration in the concentration area A_(C) may be adjusted byaltering the movement profile of the shuttle pan 404′. The movementprofile of the shuttle pan 404′ can be described as a plot of the pan'soutlet edge 406 position, relative to the stroke distance D_(S), as afunction of time. The movement profile determines how the outlet edge406 “follows” the fibrous material, and may be adjusted to move fasterthan, slower than, or at the same speed as the fibrous material atvarious locations. FIG. 19 is a plot of the movement profile for theexemplary shuttle pan 404′ of FIGS. 18A-18E. The solid curve 1900 showsthe position of the outlet edge 406 as a function of time t. The dashedcurves 1902 show the position of the leading edge of each core length X₁of fibrous material that passes below the outlet edge. The dotted line1904 is a plot of a typical SAP concentration that might result from theuse of this movement profile. FIG. 19 is meant to be exemplary, andthose skilled in the art will understand that other profiles may beused, and other SAP concentrations may be obtained using this and othermovement profiles, SAP flow rates, and so on. For example, in otherembodiments, the stroke distance DS and the duration and velocity of theforward and backward strokes may be increased or decreased to provideother profiles.

[0181] The shuttle pan's movement profile may be varied in a number ofways, such as by altering the shapes and sizes of the shuttle pan'sdrive unit and linkage or directly controlling the movement of theshuttle pan's actuating devices, as is known in the art. Other methodsof varying the location and relative concentration of SAP 326 in thefibrous material by altering the movement profile of the shuttle pan404′ will be apparent to those skilled in the art based in the teachingsherein.

[0182] Although the shuttle pan 404′ of the present invention has beendescribed herein as being used with a vibratory feeder, is should beapparent to those skilled in the art that the shuttle pan 404′ also maybe used with other types of SAP feeding devices, provided those devicesare capable of providing a relatively consistent and controllable flowof SAP. For example, the shuttle pan 404′ may be adapted as part of afixed (i.e., non-vibratory) feed tray, and the SAP 326 may be providedto the shuttle pan 404′ by an auger-type feeder, a vibratory feeder thatdoes not have a feed tray 334, or any other metered flow device. In theembodiment shown in FIG. 20, the shuttle pan 404′ is part of a fixedfeed tray 2000 that is fed by an auger-type feeder 2002 that conveys SAP(or other particulate matter) to the fixed feed tray 2000 from a SAPsupply unit 2004.

[0183] All or part of the assembly may be suspended from scales (notshown) to operate as a loss-in-weight feeder, as described elsewhereherein. Exemplary devices that may be used as the auger-type feeder 2002and scales for such an embodiment include a FLEXICON flexible screw(auger) conveyor, which may be controlled by a SOLIDSFLOW MODEL 1200LOSS-IN-WEIGHT CONTROLLER using feedback from the scales 1906. Anexemplary supply unit 2004 is the SOLIDSFLOW MODEL SBS BULK BAGDISCHARGE STATION.

[0184] In still another embodiment of the invention, the shuttle pan404′ may be part of a fixed feed tray 2000 that is located below avibratory feeder 332 or other metered feed device without being attachedto the feed device. In such an embodiment, vibrations and othermovements of the shuttle pan 404′ are not conveyed to the feed device,and so it may not be necessary to damp feed tray 2000 movements thatwould otherwise impair the use of loss-in-weight measurements.

[0185] The shuttle pan 404′ of the present invention may be used toprovide beneficial zoned absorbency to absorbent cores, both of theopened tow variety and the conventional fluffed pulp variety. Such ashuttle pan 404′ may be particularly useful when retrofitted to existingmachinery that is unable to operate quickly enough to provide zones ofhigh SAP concentration, as may be the case when high operating speedsare desired.

[0186] Other embodiments, uses, and advantages of the invention will beapparent to those skilled in the art from consideration of thespecification and practice of the invention disclosed herein. Thespecification should be considered exemplary only, and the scope of theinvention is accordingly intended to be limited only by the followingclaims and equivalents thereof.

I claim:
 1. An apparatus for depositing particulate matter onto a supplyof absorbent core fibrous substrate material moving in a machinedirection comprising: a feed tray having an inlet for receiving a supplyof particulate matter; a shuttle pan slideably positioned to form atleast part of a lower pan of the feed tray; the shuttle pan having anoutlet edge located proximal the supply of absorbent core fibroussubstrate material, the outlet edge being located so that the supply ofparticulate matter passes over the outlet edge to exit the feed tray andbe deposited on the supply of absorbent core fibrous substrate material;the shuttle pan having a range of motion comprising a forward stroke anda backward stroke, wherein during the forward stroke the outlet edgefollows the supply of absorbent core fibrous substrate material; and amechanism for moving the shuttle pan through its range of motion.
 2. Theapparatus of claim 1, wherein the supply of particulate matter is asupply of superabsorbent particles.
 3. The apparatus of claim 1, whereinthe supply of absorbent core fibrous substrate material comprises asupply of cellulose acetate tow.
 4. The apparatus of claim 1, whereinthe shuttle pan forms substantially all of the lower pan of the feedtray.
 5. The apparatus of claim 1, wherein the supply of absorbent corefibrous substrate material is conveyed by a conveying mechanism that isoffset from the outlet edge by an offset distance.
 6. The apparatus ofclaim 5, wherein the offset distance is from about 0.25 inches to about4.00 inches.
 7. The apparatus of claim 5, wherein the offset distance isfrom about 0.375 inches to about 1.00 inch
 8. The apparatus of claim 5,wherein the offset distance is from about 0.50 inches.
 9. The apparatusof claim 5, wherein the conveying mechanism is substantially parallel tothe shuttle pan.
 10. The apparatus of claim 5, wherein: the conveyingmechanism is not substantially parallel to the shuttle pan; at oneposition of the range of motion the outlet edge is offset from theconveying mechanism by a maximum offset distance; at another position ofthe range of motion the outlet edge is offset from the conveyingmechanism by a minimum offset distance; and the maximum offset distanceis not more than about 300% of the minimum offset distance.
 11. Theapparatus of claim 5, wherein the conveying mechanism is a combiningdrum.
 12. The apparatus of claim 1, wherein the range of motiontraverses a stroke distance of from about 2 inches to about 13 inches.13. The apparatus of claim 1, wherein the range of motion traverses astroke distance of from about 4 inches to about 11 inches.
 14. Theapparatus of claim 1, wherein the range of motion traverses a strokedistance of from about 6 inches to about 9 inches.
 15. The apparatus ofclaim 1, wherein the feed tray is a vibratory feed tray.
 16. Theapparatus of claim 1, wherein the feed tray is a fixed feed tray. 17.The apparatus of claim 16, further comprising a metered flow device forconveying particulate matter to the inlet.
 18. The apparatus of claim17, wherein the metered flow device is an auger-type feeder.
 19. Theapparatus of claim 1, wherein the amount of particulate matter depositedfrom the feed tray is controlled by a loss-in-weight control system. 20.A method for depositing particulate matter onto a supply of absorbentcore fibrous substrate material moving in a machine directioncomprising: supplying particulate matter to a feed tray having a shuttlepan; sliding the shuttle pan through a range of motion comprising aforward stroke and a backward stroke, wherein during the forward strokean outlet edge of the shuttle pan follows the supply of absorbent corefibrous substrate material, thereby depositing zones having a relativelyhigh concentration of particulate matter onto the absorbent core fibroussubstrate material.
 21. The method of claim 20, wherein the supply ofparticulate matter is a supply of superabsorbent particles.
 22. Themethod of claim 20, wherein the supply of absorbent core fibroussubstrate material comprises a supply of cellulose acetate tow.
 23. Themethod of claim 20, wherein sliding the shuttle pan through a range ofmotion comprises sliding the shuttle pan through a range of motion offrom about 2 inches to about 13 inches.
 24. The method of claim 20,wherein sliding the shuttle pan through a range of motion comprisessliding the shuttle pan through a range of motion of from about 4 inchesto about 11 inches.
 25. The method of claim 20, wherein sliding theshuttle pan through a range of motion comprises sliding the shuttle panthrough a range of motion of from about 6 inches to about 9 inches. 26.The method of claim 20, further comprising vibrating the feed tray. 27.The method of claim 20, wherein supplying particulate matter comprisessupplying particulate matter with a metered flow device.
 28. The methodof claim 27, wherein the metered flow device is an auger-type feeder.29. The method of claim 20, further comprising controlling the amount ofparticulate matter deposited onto the supply of absorbent core fibroussubstrate material using a loss-in-weight control system.
 30. Anabsorbent garment comprising: a topsheet; a backsheet; and an absorbentcore disposed between the topsheet and the backsheet comprising fibroussubstrate material and particulate matter; wherein the particulatematter is distributed in the fibrous substrate material using theapparatus of claim
 1. 31. The absorbent article of claim 30, wherein thefibrous substrate material comprises an opened tow of cellulose acetateand the particulate matter comprises superabsorbent particles.
 32. Anabsorbent article comprising: a topsheet; a backsheet; and an absorbentcore disposed between the topsheet and the backsheet comprising fibroussubstrate material and particulate matter; wherein the particulatematter is distributed in the fibrous substrate material using the methodof claim
 20. 33. The absorbent article of claim 32, wherein the fibroussubstrate material comprises an opened tow of cellulose acetate and theparticulate matter comprises superabsorbent particles.